Claims
- 1. An attrition mill apparatus comprising:
- a grinding chamber (1) having a grinding stage or stages ("GS");
- one or more inlets (3) for admitting into the apparatus a coarse grinding medium, a slurrying liquid, and a substance to be ground;
- an apparatus outlet (6);
- an axial impeller (10) disposed in the grinding chamber (1) and adapted to cooperate with a slurry of the medium to reduce the particle size of the substance to fine particles;
- a classifier ("CS") within the grinding chamber for classifying particles in the slurry on the basis of particle mass so that a slurry of fine particles flows to said apparatus outlet and discharges from the mill while coarse particles return to the grinding stage or stages ("GS"); and
- wherein the fine particles pass from the classifier ("CS") to said outlet (6) via at least one passage selected from the group consisting of at least one screened passage (24) and at least one unscreened passage (25), said at least one passage having a minimum passage dimension which is not only greater than the dimension of fine particles discharged, but also is greater than the D50 dimension of the equilibrium grinding medium retained in the mill.
- 2. The apparatus according to claim 1, wherein the minimum passage dimension is greater than the D80 dimension of the equilibrium grinding medium retained in the mill.
- 3. The apparatus according to claim 2, wherein the minimum passage dimension is greater than at least twice the maximum dimension of equilibrium grinding medium retained in the mill.
- 4. The apparatus according to claim 1, wherein the at least one passage (24 or 25) is screened (24) and the minimum passage dimension is a screen orifice.
- 5. The apparatus according to claim 1, wherein the grinding stage or stages are adapted to grind a substance to be ground to a fineness of at least 80% passing 16 microns.
- 6. The apparatus according to claim 1, including at least 2 grinding elements spaced apart by a distance "g" along the axial impeller wherein the classifier comprises a classification element mounted on the rotor and spaced by a distance "c" from an adjacent grinding element, wherein "c" is less than "g".
- 7. The apparatus according to claim 6, wherein "g" is selected to optimize grinding and wherein "c" is selected so as to classify the fine particles from the mixture of the coarse and the fine particles.
- 8. The apparatus as claimed in claim 6, wherein "c" is selected to permit the coarse and fine particles to circulate spirally between the periphery of the grinding elements and the impeller shaft.
- 9. The apparatus as claimed in claim 6, wherein "c" is less than 0.75 times "g".
- 10. The apparatus as claimed in claim 6, wherein "c" is less than 0.6 times "g" and greater than 0.01 times "g".
- 11. The apparatus according to claim 6, wherein "c" is less than 0.6 times "g" and greater than 0.4 times "g".
- 12. The apparatus according to claim 6, wherein the classifier element is a radially directed disk pierced by one or more openings.
- 13. The apparatus according to claim 12, wherein the classifier element is pierced by equiangularly spaced openings.
- 14. The apparatus according to claim 12, wherein the classifier element has substantially the same diameter as an adjacent grinding element.
- 15. The apparatus according to claim 1, including at least two grinding elements spaced apart by a distance "g" along the axial impeller and a first classification element spaced from a second classification element by a distance "c" which is less than "g" and wherein at least one of said classification elements is driven in axial rotation with respect to the other.
- 16. The apparatus according to claim 15, wherein said classification elements are annular disks pierced by axially extending apertures.
- 17. The apparatus according to claim 15, wherein each of the first and second classifier elements are driven in rotation independently of each other.
- 18. The apparatus according to claim 17, wherein one of the elements is driven in counter rotation to the other.
- 19. The apparatus according to claim 1, containing a grinding medium having a particle size distribution, when fed to the mill, of 80% passing at least 2.3 mm.
- 20. The apparatus according to claim 1, containing a feed to be ground having a particle size distribution D80 passing from 45 microns to 57 microns.
- 21. The apparatus according to claim 20, wherein the particle size distribution of the product is such that at least 80% of the product passes 16 micron.
- 22. The apparatus according to claim 1, further including a separator stage ("SS") defining a separator outlet (25) and a radially disposed passage (33),
- wherein the classifier has a classifier passage outlet (32), and the particles exiting the classifier via the classifier passage outlet (32) enter the radially disposed passage (33) and exit from the radially disposed passage (33) at the separator outlet (25) which is disposed radially inwardly of the classifier outlet (32).
- 23. A method for classifying particles in a slurry, comprising a substance to be ground, in an attrition mill having one or more inlets, an apparatus outlet (6), a grinding chamber having a grinding stage or stages ("GS"), an axial impeller (10) disposed in the grinding chamber and adapted to cooperate with a slurry of coarse grinding medium to reduce to fine particles the substance to be ground, comprising the steps of:
- admitting the slurry to a passage (19) having a passage inlet (15A) and a passage outlet (32) disposed opposite or radially inwards of the passage inlet (15A),
- rotating the slurry in the passage about the impeller axis, and
- selecting the velocity of rotation of the slurry having regard to the mass of coarse and fine particles in the slurry to separate the coarse particles from the fine particles so that slurry exiting from the passage outlet contains the fine particles and is substantially free of coarse particles.
- 24. The method according to claim 23, wherein the slurry is driven in a rotation by means of a pair of discs spaced apart by a distance less than the spacing between adjacent grinding elements and defining the passage therebetween.
- 25. The method according to claim 24, containing a grinding medium having a particle size distribution, when fed to the mill, of 80% passing at least 2.3 mm.
- 26. The method according to claim 24, containing a feed to be ground having a particle size distribution D80 passing from 45 microns to 57 microns.
- 27. The method according to claim 24, wherein the rotational velocity of the pair of discs in selected so that particles entrained in the slurry exiting from the radially inner passage outlet have a particle size distribution such that at least 80% pass 16 microns.
- 28. The method according to claim 23, further including a separator stage ("SS") defining a separator outlet (25) and a radially disposed passage (33),
- wherein the classifier has a classifier passage outlet (32), and the particles exiting the classifier via the classifier passage outlet (32) enter the radially disposed passage (33) and exit from the radially disposed passage (33) at the separator outlet (25) which is disposed radially inwardly of the classifier outlet (32).
- 29. The method according to claim 23, wherein the slurry exiting from said passage outlet passes through another passage including from said passage outlet to and through the apparatus outlet wherein the minimum dimension of said another passage is not only greater than the dimension of the fine particles discharged from the mill but would pass therethrough 80% of the equilibrium grinding medium content retained in the mill.
- 30. The method according to claim 29, wherein said another passage comprises a member of he group consisting of a screen having a minimum dimension for which 80% of the equilibrium grinding medium content retained in the mill is capable of passing through the screen and no screen.
- 31. A method for classifying particles in a slurry, comprising a substance to be ground, in an attrition mill having one or more inlets, an apparatus outlet (6), a grinding chamber having a grinding stage or stages ("GS"), an axial impeller (10) disposed in the grinding chamber and adapted to cooperate with a slurry of coarse grinding medium to reduce to fine particles the substance to be ground, comprising the steps of:
- admitting the slurry to a passage (19) having a passage inlet (15A) and a passage outlet (32) disposed opposite or radially inwards of the passage inlet (15A),
- rotating the slurry in the passage about the impeller axis, and
- selecting the velocity of rotation of the slurry having regard to the mass of coarse and fine particles in the slurry to separate the coarse particles from the fine particles so that slurry exiting from the passage outlet contains the fine particles and is substantially free of coarse particles,
- wherein the slurry exiting from said passage outlet passes from said passage outlet to the apparatus outlet via another passage wherein the minimum dimension is not only greater than the dimension of the fine particles discharged from the mill but also would pass therethrough 80% of the equilibrium grinding medium content retained in the mill.
- 32. A method for classifying particles in a slurry, comprising a substance to be ground, in an attrition mill having one or more inlets, an apparatus outlet (6), a grinding chamber having a grinding stage or stages ("GS"), an axial impeller (10) disposed in the grinding chamber and adapted to cooperate with a slurry of coarse grinding medium to reduce to fine particles the substance to be ground, comprising the steps of:
- admitting the slurry to a passage (19) having a passage inlet (15A) and a passage outlet (32) disposed opposite or radially inwards of the passage inlet (15A),
- rotating the slurry in the passage about the impeller axis, and
- selecting the velocity of rotation of the slurry having regard to the mass of coarse and fine particles in the slurry to separate the coarse particles from the fine particles so that slurry exiting from the passage outlet contains the fine particles and is substantially free of coarse particles,
- wherein the slurry is driven in a rotation by means of a pair of discs spaced apart by a distance less than the spacing between adjacent grinding elements and defining the passage therebetween,
- wherein the impeller includes at least two grinding elements spaced apart by a distance "g" along the axial impeller and the pair of discs is mounted on the rotor and spaced by a distance "c" from an adjacent grinding element, wherein "c" is less than 0.7 times "g".
- 33. The apparatus according to claim 32, wherein "c" is less than 0.6 times "g" and greater than 0.01 times "g".
- 34. The method according to claim 32, wherein "c" is less than 0.6 times "g" and greater than 0.4 times "g".
- 35. A method for classifying particles in a slurry, comprising a substance to be ground, in an attrition mill having one or more inlets, an apparatus outlet (6), a grinding chamber having a grinding stage or stages ("GS"), an axial impeller (10) disposed in the grinding chamber and adapted to cooperate with a slurry of coarse grinding medium to reduce to fine particles the substance to be ground, comprising the steps of:
- admitting the slurry to a passage (19) having a passage inlet (15A) and a passage outlet (32) disposed opposite or radially inwards of the passage inlet (15A),
- rotating the slurry in the passage about the impeller axis, and
- selecting the velocity of rotation of the slurry having regard to the mass of coarse and fine particles in the slurry to separate the coarse particles from the fine particles so that slurry exiting from the passage outlet contains the fine particles and is substantially free of coarse particles,
- wherein the slurry is driven in a rotation by means of a pair of discs spaced apart by a distance less than the spacing between adjacent grinding elements and defining the passage therebetween,
- wherein the coarse particles are separated from the fine particles solely by centrifugal force.
- 36. An attrition mill comprising:
- a grinding chamber having a grinding stage or stages;
- one or more inlets for admitting into the apparatus a coarse grinding medium, a slurrying liquid, and a substance to be ground;
- an apparatus outlet;
- an axial impeller disposed in the grinding chamber and adapted to cooperate with a slurry of said medium to reduce the particle size of said substance; and
- a classifying stage wherein the particles are separated for discharge from the mill from particles to be returned to the grinding stage or stages solely by centrifugal force.
Priority Claims (3)
Number |
Date |
Country |
Kind |
44 124 08 |
Apr 1994 |
DEX |
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PM 6394 |
Jun 1994 |
AUX |
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PN 0166 |
Dec 1994 |
AUX |
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Parent Case Info
The present application is a continuation-in-part of U.S. patent application Ser. No. 08/727,433, filed Oct. 11, 1996, now patented as U.S. Pat. No. 5,797,550, incorporated herein by reference in its entirety.
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EPX |
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Entry |
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Continuation in Parts (1)
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Number |
Date |
Country |
Parent |
727433 |
Oct 1996 |
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