The present invention relates to a mill for crushing stone, minerals and other materials that may be fractured. More specifically, the present invention relates to a form of rotary mill which uses high speed air as a medium to cause various materials to be broken down into smaller pieces by repeatedly colliding into each other
There is a need for machinery suitable for crushing stone, minerals and other materials that may be fractured. There is also a need for a rotary mill that can fracture hard materials by colliding the input materials into each other repeatedly to break them into successively smaller and smaller pieces. Many rock crushing and breaking machines in use today rely upon the action of hardened steel to smash and pulverize rocks and minerals into smaller pieces. These machines can achieve a particle size reduction, but these machines are subject to a great deal of wear and tear in the course of normal operation.
Rock crushing machines are further limited in the size of particles that may be input and subsequently reduced to only a certain fraction of the previous particle size at the output. Using typical rock crushing machines, to reduce rock pieces of about 2 inches in diameter (about 500 mm) into a very fine powder having particles sizes which are less than 0.002 inches in diameter (about 0.5 mm), it would be necessary to process this material in a series of steps moving from one machine to another and requiring a considerable amount of processing time and additional handling.
Accordingly, there is a need for machinery for crushing or milling stone, minerals and other materials into very small particles or fine powders. It is further desired to produce a mill that can reduce input materials to approximately 1/1000 of the original size in just a single processing step. It would also be desired to create a mill that utilizes air circulating at high speed as a primary medium by which input material is crushed without causing undue wear and tear on the mill itself, thereby greatly reducing the frequency with which parts are replaced. There is also a desire to produce such a mill that is completely scaleable in size, both upward and downward, to better accommodate lager and smaller input materials by keeping the component parts of the mill sized proportionally to one another.
The rotary collider air mill of the present invention is generally intended for application to rock, mineral or other materials that may be fractured by forcing the input materials to into a series of collisions. In short, the air mill of the present invention will create high velocity chaotic air currents within an enclosure that will force input materials to repeatedly collide with each other at very high speeds and cause the input materials to fracture into smaller and smaller pieces. In some embodiments the rotary collider air mill may be utilized in to produce cosmetic powders, food spices, building products, metallurgical products, plastic fillers and a number of other items.
In a number of exemplary embodiments of the present invention a rotary collider air mill comprising a polygonal housing having at least 5 sides, a sprocket having at least 3 blades attached thereto, a drive shaft for rotating the sprocket at high speeds, an input port and an output port is disclosed. In one embodiment of the present invention the apparatus of the present invention will be fully scalable upward or downward in volume by resizing the polygonal housing, the sprocket, and the blades proportionally to each other. By way of example only, the internal mechanisms of the sprocket and the attached arms may rotate through a space that has a diameter of 12, 18, 24, 48, 60, 96 or even 144 inches across by scaling the housing and internal mechanisms upward or downward proportionally to each other to preserve operational functionality.
In another embodiment of the present invention the rotary collider air mill will use high velocity chaotic air as a medium to repeatedly smash input materials into each other in a series of collisions to fracture the input materials into smaller and smaller pieces. In yet another embodiment of the present invention the apparatus will be capable of moving air at speeds in the transonic range of about 600 to 768 miles per hour (mph) and approaching the speed of sound. In a further embodiment of the present invention the rotary air collider mill will be able to reduce input materials to about 1/1000 of the original size in a single processing step.
By way of example only, the apparatus of the present invention may reduce input materials of about 1 to 2 inches in size to a fine powder of less than about 0.001 inches in size, a significant portion of which may be passed through a #200 mesh screen, particles having sizes of less than about 100 microns. The apparatus of the present invention represents a significant improvement and advance in technology over the existing ball mills, hammer mills, roller mills and jet mills now in use.
The present invention will be better understood in view of the detailed description in conjunction with the following figures and in which:
In one embodiment, the rotary air collider mill is an apparatus comprising a polygonal housing having at least 5 sides, a sprocket having at least 3 blades attached thereto, a drive shaft for rotating the sprocket at high speeds, an input port and an output port. These components should be precisely machined and sized proportionately to each other, but may be scaled up or down in size so long as the proportions of these components are preserved relative to one another. By way of example only, it will be possible to construct an apparatus in accordance with the present invention in which the sprocket and attached blades sweep through a diameter of about 12, 18, 24, 48, 60, 96 or 144 inches so long as the housing, sprocket, blades, drive shaft, input port and output port are all sized proportionately to each other.
One component of the rotary air collider mill is polygonal housing having at least 5 sides. The polygonal housing should be constructed of steel or similar materials that are particularly hard, durable and not brittle across a wide range of operating temperatures. The polygonal housing-should have a front plate, a back plate and at least 5 side panels. The front plate and the back plate should be placed vertically and positioned parallel to each other with the at least 5 side panels defining an enclosed volume between them. The at least 5 side panels may define a symmetrical or asymmetrical polygonal housing. By way of example only, it is possible to form useful housings for the present invention having 6, 8, 10, 12 or more side panels disposed between the front plate and the back plate.
In one embodiment of the present invention, it is possible to form a housing having 8 equally sized side plates to form a regular and symmetrical octagonal housing. This embodiment would have a cut away profile that resembles a typical “stop sign” shape that is familiar to all drivers as a traffic control device. Note that while the number of sides may vary the polygonal chamber should be oriented such that the bottom most portion is a flat side panel rather than a joint between two sides. This is intended to ensure that the rotating sprocket and attached blades will completely sweep the bottom of the apparatus when rotated and avoid an accumulation of rock or mineral debris at the bottom of the housing. The accumulation of rock or mineral debris within the housing would require cleaning and removal to prevent damage to the apparatus and could be rather time consuming.
By way of example only, a suitable housing for a rotary collider air mill with a 48 inch diameter and a regular octagonal chamber will now be described herein in some detail. Referring now to both
Still referring to both
As shown in
Still referring to
It is critical that the input port 114 be located within the 24 inch radius defined by the rotation of the sprocket and attached blades, not shown here, minus the displacement of the blades themselves. In short, the input port 114 must be located between the outer radius of the drive shaft (about 2 inches from center) and the innermost radius defined by the moving blades (about 22 inches from center). As shown in
Referring now to
Referring now to both
Referring now to
The drive shaft 200 is connected to a drive motor, not shown, which may be a gas, diesel or electric power source which is then connected to the drive shaft 200 by means of belts, gears or other transmissions to permit the drive shaft 200 to rotate at various speeds, as needed. The drive motor or power source is not specified with particularity here because it may take many different forms and may be rated at various levels of horsepower (hp) which need only to be sufficient to drive the apparatus at the desired number of revolutions per minute (rpm). By way of example only, a rotary collider air mill of 48 inches in diameter will typically operate at about 100 to about 5000 revolutions per minute. This type of operation would usually require a motor having a power rating of approximately 10 to 250 horsepower. By way of example only, a 125 horsepower motor turning at about 4800 rpm could produce blade speeds reaching about 660 miles per hour on a 48 inch diameter model.
Referring now to
Still referring to
As shown here, each arcuate blade section 315, 325, 335 is mounted on a pair of parallel arms 310, 320, 330 that extend radially outward from the hub 305 or central portion of the sprocket 300. Although a pair of parallel arms are shown here, it is to be understood that each arcuate blade section 315, 325, 335 may be attached to the sprocket 300 by one arm, two arms, three arms or more. The arcuate blade section 315, 325, 335 may be mounted or welded to the pair of arms 310, 320, 330 at any angle ranging from about 0 to 60 degrees (half of 120 degrees) to alter or adjust the angle of attack with which the leading edge of the blade will meet the air inside the polygonal housing 100. The angle at which the blade is mounted to the arms not only determines the angle of attack with the air within the housing but also helps to define the displacement of the blade. As noted earlier, the displacement of the blade is the difference between the outermost radius swept by the rotating blade and the innermost radius swept by the rotating blade. As shown in
The displacement will be minimized when the blade is mounted at 0 degrees and will be maximized when the blade is mounted at 60 degrees. Accordingly, the more the blade is rotated to cup or catch the oncoming air, the greater the displacement of the blade. It is notable that the largest blade displacement is not always the most desirable configuration in when the air mill is in operation. In some cases, it may be desirable to reduce the displacement of the blades to increase the residence time of the input materials within the housing. Input materials which remain in the housing for longer periods of time will usually experience more collisions and produce smaller output particle sizes.
Referring now to
The removable parallel arm and blade units would be particularly useful if one of the attached blade sections were to become severely damaged and in need of replacement. In this way, it would be possible to replace a just single blade section by removing two retaining pins rather than having to replace the entire sprocket and all of the attached blade sections at once. This alternative embodiment would also permit air mill operators to switch out the parallel arm and blade units to change the angle or the shape of the blades. Although the blade sections illustrated herein are three 120 degree arcuate portions that are formed from a single steel pipe, it is to be understood that the blade sections may have different thickness, radius of curvature or even be somewhat flattened out, if desired.
Another alternative embodiment of the present invention is contemplated by having a sprocket with welded or fixed arms and having removable blades attached to the arms by a number of small removable pins. In brief, rather than removing the entire arm and blade units as shown in
While a number of preferred embodiments of the invention have been shown and described herein, modifications may be made by one skilled in the art without departing from the spirit and the teachings of the invention. The embodiments described herein are exemplary only, and are not intended to be limiting. Many variations, combinations, and modifications of the invention disclosed herein are possible and are within the scope of the invention. Accordingly, the scope of protection is not limited by the description set out above, but is defined by the claims which follow, that scope including all equivalents of the subject matter of the claims.
This application claims priority to U.S. Provisional Patent Application No. 61/965,078 entitled “Rotary Collider Air Mill” and filed on Jan. 22, 2014. The provisional application is hereby incorporated in its entirety by specific reference thereto.
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Number | Date | Country | |
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20150202631 A1 | Jul 2015 | US |
Number | Date | Country | |
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61965078 | Jan 2015 | US |