US3180582A - Bowl for centrifugal pulverizer - Google Patents
Bowl for centrifugal pulverizer Download PDFInfo
- Publication number
- US3180582A US3180582A US287304A US28730463A US3180582A US 3180582 A US3180582 A US 3180582A US 287304 A US287304 A US 287304A US 28730463 A US28730463 A US 28730463A US 3180582 A US3180582 A US 3180582A
- Authority
- US
- United States
- Prior art keywords
- bowl
- impeller
- particles
- wall
- angle members
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/14—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices
- B02C13/18—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices with beaters rigidly connected to the rotor
- B02C13/1807—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices with beaters rigidly connected to the rotor the material to be crushed being thrown against an anvil or impact plate
- B02C13/1835—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices with beaters rigidly connected to the rotor the material to be crushed being thrown against an anvil or impact plate by means of beater or impeller elements fixed in between an upper and lower rotor disc
- B02C13/1842—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices with beaters rigidly connected to the rotor the material to be crushed being thrown against an anvil or impact plate by means of beater or impeller elements fixed in between an upper and lower rotor disc with dead bed protected beater or impeller elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/14—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices
- B02C13/18—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices with beaters rigidly connected to the rotor
- B02C13/1807—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices with beaters rigidly connected to the rotor the material to be crushed being thrown against an anvil or impact plate
- B02C13/1814—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices with beaters rigidly connected to the rotor the material to be crushed being thrown against an anvil or impact plate by means of beater or impeller elements fixed on top of a disc type rotor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/14—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices
- B02C13/18—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices with beaters rigidly connected to the rotor
- B02C13/1807—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices with beaters rigidly connected to the rotor the material to be crushed being thrown against an anvil or impact plate
- B02C2013/1857—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices with beaters rigidly connected to the rotor the material to be crushed being thrown against an anvil or impact plate rotating coaxially around the rotor shaft
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/14—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices
- B02C13/18—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices with beaters rigidly connected to the rotor
- B02C13/1807—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices with beaters rigidly connected to the rotor the material to be crushed being thrown against an anvil or impact plate
- B02C2013/1885—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices with beaters rigidly connected to the rotor the material to be crushed being thrown against an anvil or impact plate of dead bed type
Definitions
- This invention relates to centrifugal pulverizers for reducing the particle size of materials, such as ore, rock, pigment, clay and the like.
- the invention relates particularly to an improved bowl for such a centrifugal pulver-
- the type of centrifugal pulverizer referred to above generally includes an impeller which is driven rotationally athigh speed about a vertical axis.
- the impeller is generally supported ⁇ at the bottom end and the material to be crushed is dropped down into the impeller through a Stationary vertical feed tube located above the impeller on the center axis of rotation. The material enters the impeller near the center axis and is propelled outwardly by centrifugal force.
- the impeller is mounted for rotation within a bowl which is also generally mounted for rotation, but at a much lower speed than the impeller and preferably in the opposite direction.
- the material propelled outwardly by the rapidly rotating impeller is projected against the walls of the bowl, and unless some form of protection is provided the walls are subjected to rapid wear and erosion.
- the object of my present invention is to provide an improved bowl construction, particularly with respect to the impact area of the bowl.
- FIG. 2 is a top plan view of the bowl of FiG. 1 lool;- ing down along the line II-ll of FIG. 1.
- FIG. 1 shows a section of the housing 2li of a centrifugal impeller.
- a bearing housing 2S which supports an impeller drive shaft 26 and a bowl drive spindle 27.
- the impeller 4t is rotated in the counterclockwise direction, as viewed in FIG. 2 and the bowl 6) is rotated in the clockwise direction, as indicated by the arrows.
- the impeller shaft 26 may be driven by a motor (not shown) through drive belts (not shown) attached to the sheave 29, while the.
- bowl spindle 27 may be driven by a motor (not shown) through a drive belt (not shown) attached'to the sheave 31.
- the bowl 6d is illustrated in FIG. 1 as comprised of two sections, a lower section 61, and an upper section 62.
- the upper section 62 is illustrated as having a horizontal portion 63 and a lip portion 64.
- the horizontal portion 63 is bolted to the wall 34 of the lower section. rfhe "ice lip portion 64 inclines outward at an angle preferably of 33 relative to the vertical, for a reason to be mentioned later.
- Bowl otl' is supported on the spindle 27 and has a central axial opening in its iloor through which the impeller drive shaft 25 passes.
- the circumferential wall 34 of the lower section 61 is vertical.
- annular depression or trough 35 In the oor of the lower section 61, intermediate the main wall 3d and the bearing housing 25, is an annular depression or trough 35; and between the trough 36 and the bearing housing 25 are a plurality of radial vents 37.
- the impeller 49 is mounted within the bowl oli on the impeller drive shaft 26.
- the mpeller d@ may be a single-deck affair, but is illustrated in FlG. 1 as having two decks formed by the three impeller discs, the upper disc 41, the middle disc 42 and the lower disc 43. vertically disposed between each set of discs are a plurality of radial webs or varies 44, which may be secured to the discs as by bolts.
- These impeller vanes 44 as seen in FIG. 2, curve in the direction of rotation of the impeller, and when the irnpeller is rotated at high speed, the vanes 4d eject the particles outwardly by centrifugal force.
- the ejected particles are thrown at high speed toward the wall 34 of the impeller bowl, and, unless intercepted, would strike the inner surface of the wall 34 with great forces tending to cause rapid wear of the wall.
- the wall 3d of the bowl 60 is protected by an annular impactor ring 5d.
- lmpactor ring 50 is formed of a plurality of angle members 51, preferably steel, placed in abutting positions in a continuous annular recess 38 formed in the iioor of the bowl 6) immediately in front of the wall 34.
- angle members 5l comprise a radial leg S2 and a circumferential leg S3, and are so positioned inthe annular recess 38 that their radial legs 52 face in the direction of rotation of the bowl, clockwise as viewed in FIG. l.
- the angle members are clamped in place by the horizontal portion 63 of the upper section 62 but are otherwise unsecured.
- the particles of material such as ore, rock, pigment, clay, etc., which are to be reduced in size, are fed, as from a hopper (not shown) into a vertically disposed stationary feed tubeV (not shown) and are dropped down, as indicated by the arrow 55, into the center region of the impeller fill.
- These particles fall into the lower deck of the impeller 4t), and as the impeller is rotated at high speed, which may be of the order of 2290-3600 rpm., the particles are thrown by the impeller vanes i4 outwardly in the direction of the impactor ring 5d formed by the angle members S1.
- the iii-st particles to be ejected strike the angle members 51, and tend to be retained within the pockets 54, formed by the angle members 51,'due tol the centrifugal force established by rotation of the bowl which, in a typical case, may be a speed of from 300 to 450 r.p.m.
- the pockets 54 tend to fill up with the particles, thus forming a protective coating protecting the angle plates 51 fromwear.
- the particles ejected thereafter which are sufficiently crushed and reduced in size by their own impact against the'wall andmadeira by the impact of other later-arriving particles, begin to climb up the inclined lip de of the impeller bowl and to form a thin layer on the inner surface thereof.
- an angle of inclination of 35 relative to the vertical is the most steep angle that will permit the particles to climb up the wall, and that if the Y wall be steeper than 35 the particles of material will have to build up in the impact area and on the bowl lip until an angle of 35 is reached. Accordingly, I prefer to give the lip 54 an'angle of inclination of 33.
- angle members 51 are not bolted or otherwise fastened to the bowl or bowl wall. Angle members 51 are merely inserted in the recess 38 in abutting relationship in the position illustrated and described, forming the substantially continuous protecting ring Stb.
- the useful life of the angle members 5l is considerably extended by the Vfact that they are fully protected by the layer of particles formed thereon by the early-arriving particles which, duc to the rotational movement of the bowl, tend to be retained in the pockets 54, following which they become firmly packed due to the impact of the later arriving particles from the impeller.
- the particles are ordinarily so tightly packed in the pockets Si that, when the impeller is shut down and the bowl 32 stops rotating, the majority of the particlesrernain in the pockets 54.
- An impeller bowl for a centrifugal pulverizer in which an impeller is mounted for rotation within a bowl which is also mounted for rotation, and the impeller is adapted to project particles of material toward ytlie wall of the bowl, said impeller and bowl having means for driving them rotationally at substantially diiterent speeds, the irnpeller speed being,y much higher, said bowl having a circumferential vertical .wall and means for forming a continuous circumferential bed ⁇ of packed particles of material inside said wall .against which the subsequently projected particles of material are directed,
- Asaid last-named means comprising: an annular recess in the iloor of said bowl immediately in front of said wall, a Vplurality ot' angle members positioned edgewise in said recess in abutting relation to each other to'fo'rm a substantially continuous circumferential impactor ring of radial pockets, and means clamping said angle members in said abutting relation, said clamping means includingy an upwardly
Description
April 27, 1965 o. DANYLU KE 3,180,582
BOWL FOR CENTRIFUGAL PULVERIZER Filed June 12, 1963 INVEN TOR.
BYJ# 62j ATZ'NEYS United States Patent O 3,130,582 BGWL FR CENTRIFUGAL PULVEREZER Ostap Dany/luke. Newtown Square, Pa., assigner to Bath Iron Works Corporation, Bath, Maine, a corporation of Maine Filed June 12, 1963, Ser. No. 287,304 1 Claim. (Cl. 241--275) This invention relates to centrifugal pulverizers for reducing the particle size of materials, such as ore, rock, pigment, clay and the like. The invention relates particularly to an improved bowl for such a centrifugal pulver- The type of centrifugal pulverizer referred to above generally includes an impeller which is driven rotationally athigh speed about a vertical axis. The impeller is generally supported `at the bottom end and the material to be crushed is dropped down into the impeller through a Stationary vertical feed tube located above the impeller on the center axis of rotation. The material enters the impeller near the center axis and is propelled outwardly by centrifugal force.
In the type of centrifugal pulverizer contemplated by the present invention, the impeller is mounted for rotation within a bowl which is also generally mounted for rotation, but at a much lower speed than the impeller and preferably in the opposite direction. The material propelled outwardly by the rapidly rotating impeller is projected against the walls of the bowl, and unless some form of protection is provided the walls are subjected to rapid wear and erosion.
In my earlier filed co-pending application, Serial No. 181,552, filed March 22, 1962, entitled Centrifugal Pulverizer, the walls of the bowl are inclined outwardly upwardly. An annular recess is provided in the inner wall of the bowl at the level of the impeller and it isV intended that this ll up with particles projected from the impeller to form a protective layer for receiving the impact of subsequent particles ejected from the impeller.
The object of my present invention is to provide an improved bowl construction, particularly with respect to the impact area of the bowl.
My invention will be clear from the following detailed description of a preferred form thereof, illustrated in the drawing in which: j
(PEG. l isan elevational View, partly in section, showing an improved bowl, according to my present invention, and
FIG. 2 is a top plan view of the bowl of FiG. 1 lool;- ing down along the line II-ll of FIG. 1.
Referring now to the drawing, FIG. 1 shows a section of the housing 2li of a centrifugal impeller. Mounted on an interior floor 21 of the housing 2t) is a bearing housing 2S which supports an impeller drive shaft 26 and a bowl drive spindle 27. Shaft'Z and spindle 27, which are mounted concentrically on the vertical axis of the housing 20, are adapted to be driven independently, preferably in opposite directions and at different speeds. In the drawing, it will be assumed that the impeller 4t) is rotated in the counterclockwise direction, as viewed in FIG. 2 and the bowl 6) is rotated in the clockwise direction, as indicated by the arrows. The impeller shaft 26 may be driven by a motor (not shown) through drive belts (not shown) attached to the sheave 29, while the.
The bowl 6d is illustrated in FIG. 1 as comprised of two sections, a lower section 61, and an upper section 62. The upper section 62 is illustrated as having a horizontal portion 63 and a lip portion 64. The horizontal portion 63 is bolted to the wall 34 of the lower section. rfhe "ice lip portion 64 inclines outward at an angle preferably of 33 relative to the vertical, for a reason to be mentioned later.
Bowl otl'is supported on the spindle 27 and has a central axial opening in its iloor through which the impeller drive shaft 25 passes. The circumferential wall 34 of the lower section 61 is vertical. l
In the oor of the lower section 61, intermediate the main wall 3d and the bearing housing 25, is an annular depression or trough 35; and between the trough 36 and the bearing housing 25 are a plurality of radial vents 37.
The impeller 49 is mounted within the bowl oli on the impeller drive shaft 26. So far as the present invention is concerned the mpeller d@ may be a single-deck affair, but is illustrated in FlG. 1 as having two decks formed by the three impeller discs, the upper disc 41, the middle disc 42 and the lower disc 43. vertically disposed between each set of discs are a plurality of radial webs or varies 44, which may be secured to the discs as by bolts. These impeller vanes 44, as seen in FIG. 2, curve in the direction of rotation of the impeller, and when the irnpeller is rotated at high speed, the vanes 4d eject the particles outwardly by centrifugal force.
The ejected particles are thrown at high speed toward the wall 34 of the impeller bowl, and, unless intercepted, would strike the inner surface of the wall 34 with great forces tending to cause rapid wear of the wall.
In accordance with my present invention, the wall 3d of the bowl 60 is protected by an annular impactor ring 5d. lmpactor ring 50 is formed of a plurality of angle members 51, preferably steel, placed in abutting positions in a continuous annular recess 38 formed in the iioor of the bowl 6) immediately in front of the wall 34.
y As illustrated in the drawing, angle members 5l comprise a radial leg S2 and a circumferential leg S3, and are so positioned inthe annular recess 38 that their radial legs 52 face in the direction of rotation of the bowl, clockwise as viewed in FIG. l. The angle members are clamped in place by the horizontal portion 63 of the upper section 62 but are otherwise unsecured.
When the bowl 6d is rotated, forces are generated which tend to turn the angle members 51 in a clockise direction pivotally about the junction of their two legs, but the angle members are prevented from so rotating by the circumferential leg 53 which abuts against the wall 34 of the bowl 6d.
ln operation, the particles of material, such as ore, rock, pigment, clay, etc., which are to be reduced in size, are fed, as from a hopper (not shown) into a vertically disposed stationary feed tubeV (not shown) and are dropped down, as indicated by the arrow 55, into the center region of the impeller fill. These particles fall into the lower deck of the impeller 4t), and as the impeller is rotated at high speed, which may be of the order of 2290-3600 rpm., the particles are thrown by the impeller vanes i4 outwardly in the direction of the impactor ring 5d formed by the angle members S1. The iii-st particles to be ejected strike the angle members 51, and tend to be retained within the pockets 54, formed by the angle members 51,'due tol the centrifugal force established by rotation of the bowl which, in a typical case, may be a speed of from 300 to 450 r.p.m. As subsequent particles are ejected from the impeller, the pockets 54 tend to fill up with the particles, thus forming a protective coating protecting the angle plates 51 fromwear. Y
After the particles retained in the pockets 54 have built up to a thickness greater than'the lengthof the radial legs 52 and suicient to present a wall of tightly-packed particles inside the innermost point of upper lip 64, the particles ejected thereafter, which are sufficiently crushed and reduced in size by their own impact against the'wall andmadeira by the impact of other later-arriving particles, begin to climb up the inclined lip de of the impeller bowl and to form a thin layer on the inner surface thereof. l have found from experience that an angle of inclination of 35 relative to the vertical is the most steep angle that will permit the particles to climb up the wall, and that if the Y wall be steeper than 35 the particles of material will have to build up in the impact area and on the bowl lip until an angle of 35 is reached. Accordingly, I prefer to give the lip 54 an'angle of inclination of 33.
It will be understood that the angle members 51 are not bolted or otherwise fastened to the bowl or bowl wall. Angle members 51 are merely inserted in the recess 38 in abutting relationship in the position illustrated and described, forming the substantially continuous protecting ring Stb. The useful life of the angle members 5l is considerably extended by the Vfact that they are fully protected by the layer of particles formed thereon by the early-arriving particles which, duc to the rotational movement of the bowl, tend to be retained in the pockets 54, following which they become firmly packed due to the impact of the later arriving particles from the impeller. The particles are ordinarily so tightly packed in the pockets Si that, when the impeller is shut down and the bowl 32 stops rotating, the majority of the particlesrernain in the pockets 54.
While in FIG. 1, I have illustrated the bowl et? as having an upper inclined wall or lip 64, such upper lip 615 may, in certain instances, be `omitted and the particles allowed to be thrown out from the rotating bowl immediately above the horizontal retaining portion 63, which is needed as a retaining means for the angle members dlr.
While the preferred embodiment of this invention has been described in some detail, it will be obvious to one skilled in the art that various modifications may be made without departing from the invention as hereinafter claimed.
Having described my invention, I claim:
An impeller bowl for a centrifugal pulverizer in which an impeller is mounted for rotation within a bowl which is also mounted for rotation, and the impeller is adapted to project particles of material toward ytlie wall of the bowl, said impeller and bowl having means for driving them rotationally at substantially diiterent speeds, the irnpeller speed being,y much higher, said bowl having a circumferential vertical .wall and means for forming a continuous circumferential bed `of packed particles of material inside said wall .against which the subsequently projected particles of material are directed, Asaid last-named means comprising: an annular recess in the iloor of said bowl immediately in front of said wall, a Vplurality ot' angle members positioned edgewise in said recess in abutting relation to each other to'fo'rm a substantially continuous circumferential impactor ring of radial pockets, and means clamping said angle members in said abutting relation, said clamping means includingy an upwardly outwardly inclined lip, each of said angle members being positioned and clamped to have one leg `adjacent the circumferential wall of the bowl andthe other leg extending radially inward toward the center axis of saidpbowl, said bowl speed being suicicnt forV retaining in place said circumferential'bed ot packed particles of material and for causing the particles projected thereagainst to climb up said circumferential bed to beyond the yupper limit of said lip.
lleierences Cited by the Examiner UNITED SATES PATENTS 1,941,770 l/'MV Welsford et al. 241-275 2,562,560 7/51 Macartney L'l1-275 X 2,637,502 5/53 Bond 241-2'75 2,981,489 4/61' HannumY 241-275 2,992,784 7/ 61 Behnke et al 24l-275 ANDREW R. JUHASZ, Primary Examiner.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US287304A US3180582A (en) | 1963-06-12 | 1963-06-12 | Bowl for centrifugal pulverizer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US287304A US3180582A (en) | 1963-06-12 | 1963-06-12 | Bowl for centrifugal pulverizer |
Publications (1)
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US3180582A true US3180582A (en) | 1965-04-27 |
Family
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US287304A Expired - Lifetime US3180582A (en) | 1963-06-12 | 1963-06-12 | Bowl for centrifugal pulverizer |
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Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1253562B (en) * | 1965-12-08 | 1967-11-02 | Miag Muehlenbau | Impact and Schaelmuehle with at least two centrifugal wheels rotating around a vertical axis |
US3511446A (en) * | 1967-04-13 | 1970-05-12 | Carl L Johnson | Apparatus for processing ore |
US3869090A (en) * | 1972-07-27 | 1975-03-04 | Air Liquide | Comminuting apparatus and method |
US3888426A (en) * | 1973-08-06 | 1975-06-10 | Joe R Urschel | Machine and method for comminuting products |
EP0053882A1 (en) * | 1980-12-02 | 1982-06-16 | Taiyo Chuki Co., Ltd. | Apparatus for regenerating foundry moulding sand |
US4756484A (en) * | 1986-09-22 | 1988-07-12 | Nordberg, Inc. | Vertical shaft impact crusher with interchangeable crusher ring segments |
US4921173A (en) * | 1985-09-17 | 1990-05-01 | Bartley Bryan A | Methods of mineral breaking and apparatus used therefor |
WO1993002797A1 (en) * | 1991-08-06 | 1993-02-18 | Reichner Thomas W | Fluidized impact mill |
US5474238A (en) * | 1990-01-31 | 1995-12-12 | Buehler Ag | Impact detacher |
NL1000114C2 (en) * | 1995-04-11 | 1996-10-14 | Johannes Petrus Andreas Joseph | Multiple rotary impact breaker. |
US5662282A (en) * | 1995-02-20 | 1997-09-02 | F. Kurt Retsch Gmbh & Co. Kg | Centrifugal mill with exchangeable cassette |
US11298703B2 (en) | 2016-01-13 | 2022-04-12 | Torxx Kinetic Pulverizer Limited | Modular pulverizer |
US11440021B2 (en) | 2016-01-15 | 2022-09-13 | Torxx Kinetic Pulverizer Limited | Pulverizer system |
US11958054B2 (en) | 2018-07-12 | 2024-04-16 | Torxx Kinetic Pulverizer Limited | Pulverizer systems and methods for pulverizing material |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1941770A (en) * | 1931-03-17 | 1934-01-02 | Hubert G Welsford | Crusher |
US2562560A (en) * | 1946-01-18 | 1951-07-31 | John H Macartney | Apparatus for centrifugal pulverizing and separating |
US2637502A (en) * | 1949-06-07 | 1953-05-05 | Allis Chalmers Mfg Co | Pocketed hammer rotor for pulverizing machines |
US2981489A (en) * | 1960-02-15 | 1961-04-25 | Jr William B Hannum | Reduction apparatus |
US2992784A (en) * | 1959-02-24 | 1961-07-18 | Simplicity Eng Co | Bowl liners for crushers |
-
1963
- 1963-06-12 US US287304A patent/US3180582A/en not_active Expired - Lifetime
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1941770A (en) * | 1931-03-17 | 1934-01-02 | Hubert G Welsford | Crusher |
US2562560A (en) * | 1946-01-18 | 1951-07-31 | John H Macartney | Apparatus for centrifugal pulverizing and separating |
US2637502A (en) * | 1949-06-07 | 1953-05-05 | Allis Chalmers Mfg Co | Pocketed hammer rotor for pulverizing machines |
US2992784A (en) * | 1959-02-24 | 1961-07-18 | Simplicity Eng Co | Bowl liners for crushers |
US2981489A (en) * | 1960-02-15 | 1961-04-25 | Jr William B Hannum | Reduction apparatus |
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1253562B (en) * | 1965-12-08 | 1967-11-02 | Miag Muehlenbau | Impact and Schaelmuehle with at least two centrifugal wheels rotating around a vertical axis |
US3511446A (en) * | 1967-04-13 | 1970-05-12 | Carl L Johnson | Apparatus for processing ore |
US3869090A (en) * | 1972-07-27 | 1975-03-04 | Air Liquide | Comminuting apparatus and method |
US3888426A (en) * | 1973-08-06 | 1975-06-10 | Joe R Urschel | Machine and method for comminuting products |
EP0053882A1 (en) * | 1980-12-02 | 1982-06-16 | Taiyo Chuki Co., Ltd. | Apparatus for regenerating foundry moulding sand |
US4921173A (en) * | 1985-09-17 | 1990-05-01 | Bartley Bryan A | Methods of mineral breaking and apparatus used therefor |
US4756484A (en) * | 1986-09-22 | 1988-07-12 | Nordberg, Inc. | Vertical shaft impact crusher with interchangeable crusher ring segments |
US5474238A (en) * | 1990-01-31 | 1995-12-12 | Buehler Ag | Impact detacher |
US5280857A (en) * | 1991-08-06 | 1994-01-25 | Reichner Thomas W | Fluidized impact mill |
WO1993002797A1 (en) * | 1991-08-06 | 1993-02-18 | Reichner Thomas W | Fluidized impact mill |
US5662282A (en) * | 1995-02-20 | 1997-09-02 | F. Kurt Retsch Gmbh & Co. Kg | Centrifugal mill with exchangeable cassette |
NL1000114C2 (en) * | 1995-04-11 | 1996-10-14 | Johannes Petrus Andreas Joseph | Multiple rotary impact breaker. |
WO1996032197A1 (en) * | 1995-04-11 | 1996-10-17 | Van Den Zanden, Rosemarie, Johanna | Multiple rotary impact crusher |
US11298703B2 (en) | 2016-01-13 | 2022-04-12 | Torxx Kinetic Pulverizer Limited | Modular pulverizer |
US11440021B2 (en) | 2016-01-15 | 2022-09-13 | Torxx Kinetic Pulverizer Limited | Pulverizer system |
US11958054B2 (en) | 2018-07-12 | 2024-04-16 | Torxx Kinetic Pulverizer Limited | Pulverizer systems and methods for pulverizing material |
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