In general, the present invention relates to industrial processing machines that are used to form powder into compressed substrates or ribbons that are later granulized into particles of a particular size. More particularly, the present invention relates to systems that can form powders into a compressed substrate that has a density throughout its form that falls within a controlled range.
In many industries, dry granulated materials are utilized in the production of products. For example, in the pharmaceutical industry, dry compounds are often mixed and granulated before being formed into tablets. Similarly, in the manufacture of batteries, dry mixtures are granulated for use in the formation of cathode pellets. Regardless of the eventual use of the granulated material, the formation of the granulated material is typically made by mixing the required materials together in powdered form. The dry mix is then compacted into a substrate or ribbon. The compacted substrate is then subsequently granulated to produce granulated particles for use in production. If the size and density of the granulated particles is important in the production process, then the granulated particles are typically mechanically filtered to remove any particle that is too large or too small for use in production. Granulated particles that are too large or too small must be disposed of or reworked, therein complicating the production procedure. The use of mechanical filtering is good for collecting granulated particles of the same general size, but it does little to separate granulated particles of different densities. Accordingly, the issue of density is addressed in the process of forming the compressed substrate that is granulated. If the compressed substrate has a generally uniform density, then particles made from that compressed substrate will also have the same generally uniform density.
Having particles of a comparable size and density can be critical in many manufacturing processes. For example, in forming pharmaceutical tablets, the use of granulated particles having the same general size and density ensures that each of the tablets made contains the same amounts of active ingredients. The use of granulated particles having the same general size and density also ensures that each tablet will dissolve in the body at the same general rate, therein administering the active ingredients evenly over time.
Obtaining granulated particles of a controlled particle size can be achieved using mechanical filtration techniques. However, controlling the density of the granulated particles is more problematic. This is especially true if the powdered materials being combined have a high degree of particle cohesion. If the particles are highly cohesive, they form clumps when pressed together. If the powdered material is stirred or moved by an auger, the blades of the stirrer or auger produce localized areas of higher compressive forces that produce clumps of higher density in the powdered material. Likewise, if the powder material is compressed in a roller compactor, when static roll side seal are used, the compacted ribbon's ends tends to be less dense next to the side seals than at the center of the ribbon. Conversely, when roller attached rotating dam ring side seals are used, the compacted ribbon's ends tends to be more dense next to the side seal than at the center of the ribbon.
In U.S. Pat. No. 7,247,013 to Roland, a processing machine is disclosed that subjects powdered material to shear forces prior to passing through the rollers of a roller compactor. The shear forces disrupt the material and help disperse areas of uneven density prior to roller compression. Although the Roland system is effective, it leaves room for improvement.
The present invention improves upon the system shown in U.S. Pat. No. 7,247,013 by disrupting the powdered material with mechanical contact in addition to applying shear forces. The improved system also prevents undesirable pressures created by powder backflow buildup. These improvements are embodied by the present invention as described and claimed below.
The present invention is a system and method for processing powdered materials. The system has a first roller and a second roller. A compression zone for compressing the powdered material is disposed between the first roller and the second roller.
At least one oscillating guide plate is provided. Each guide plate has a curved edge that face the first roller. Accordingly, a curved channel is formed between the curved edge of each oscillating guide plates and the first roller. The curved channel tapers from a wide entrance opening to a narrower exit opening. The exit opening leads into the compression zone between the rollers.
The curved channel receives the powdered material and both shears and redistributes the powdered material as the powdered material advances from the wide entrance to the narrower exit. Furthermore, since part of the curved channel is made from one or more oscillating plate edges, the oscillation further shears the powdered material as it is advanced and transitioned to a thin rectangular cross section, while maintaining the powder's ability to redistribute to a more uniform density. The result is that a ribbon of powdered material with generally uniform density is produced and fed into the compression Nip zone between the rollers. The roller applies even compression to the powdered material, resulting in a compressed substrate of generally uniform density.
For a better understanding of the present invention, reference is made to the following description of exemplary embodiments thereof, considered in conjunction with the accompanying drawings, in which:
Although the present invention powder processing machine and methodology can be embodied in many ways, only a few exemplary embodiments are illustrated. The exemplary embodiments are shown for the purposes of explanation and description. The exemplary embodiments are selected in order to set forth some of the best modes contemplated for the invention. The illustrated embodiments, however, are merely exemplary and should not be considered limitations when interpreting the scope of the appended claims.
Referring to
The powder processing machine 10 is a variant of a roller compactor. In a roller compactor, material is compressed between two rollers. Using terms of art, a roller compactor has a nip zone between the rollers where the material being worked is moving at the same speed as the rollers. Just prior to the nip zone is a slip zone, where the material being worked begins to accelerate to the speed of the roller. In the powder processing machine 10, there is a slip zone 13 that approaches the two opposing rollers 16, 18 and nip zone 15 that is between the two opposing rollers 16, 18. In combination, the slip zone 13 and the nip zone 15 are herein referred to as the compression zone 14 of the powder processing machine 10. The powdered material 11 is compressed in a compression zone 14. The opposing rollers 16, 18 include a first roller 16 and a second roller 18 that rotate in opposite directions. Either one or both of the opposing rollers 16, 18 can be powdered and caused to rotate. The speed of rotation is controlled for a purpose that is later explained.
In the first exemplary embodiment of the powder processing machine 10, a plurality of oscillating guide plates 20 are disposed above the first roller 16. Each of the oscillating guide plates 20 is a planar plate defined within four primary side edges. Each guide plate 20 has a top edge 22, a bottom contact edge 24, a forward edge 26 and a distal edge 28. Within the powder processing machine 10, the contact edge 24 faces the first roller 16. The contact edge 24 is curved and extends from the forward edge 26 to the distal edge 28. The contact edge 24 meets the forward edge 26 at a sharpened salient point, therein forming an agitation tooth 30 on each oscillating guide plate 20. Each agitation tooth 30 is disposed just above the compression zone 14 between the first roller 16 and the second roller 18.
The curvature of the contact edge 24 on each oscillating guide plate 20 is longer and larger than the external curvature of the first roller 16. Consequently, the contact edge 24 near the forward edge 26 is closer to the first roller 16 than is the contact edge 24 near the distal edge 28. As a result, a curved channel 32 is formed between the first roller 16 and the contact edges 24 of the oscillating guide plates 20. The curved channel 32 is defined by the exterior of the first roller 16 and the multiple contact edges 24 of the oscillating guide plates 20. The curved channel 32 is tapered in addition to being curved. The curved channel 32 has a wide entrance opening 34 under the distal edges 28 of the oscillating guide plates 20 and a much narrower exit opening 36 under the forward edges 26 of the oscillating guide plates 20. The exit opening 36 feeds directly into the compression zone 14 between the first roller 16 and the second roller 18.
The wide entrance opening 34 of the curved channel 32 leads into a supply conduit 38. The supply conduit 38 contains an auger screw 40 or similar mechanism that can actively advance material from the supply conduit 38 to the curved channel 32. The supply conduit 38 is connected to an external hopper 42 that holds and supplies the powdered material 11.
Referring to
The eccentric drive shafts 54, 56 are rotated either in the same direction or in opposite directions to move the oscillating guide plates 20. As the eccentric dive shafts 54, 56 rotate, they function as cams and articulate the first plate set 44 and the second plate set 46 both up and down and back and forth. Referring to
Referring to
Referring now to
As the powdered material 11 is advanced into the curved channel 32, the powdered material 11 transitions from the round feed tube cross section to a thinning rectangular cross section by the converging taper of the curved channel 32. The top of the curved channel 32 that is defined by the contact edges 24 of the oscillating guide plates 20 is longer than the bottom of the curved channel 32 defined by the first roller 16. Furthermore, the first roller 16 rotates, therein advancing the powdered material 11 into the curved channel 32. As a result, the powdered material 11 at the bottom of the curved channel 32 travels faster than the powdered material 11 at the top of the curved channel 32. This produces significant shear forces in the powdered material 11 that shears the powdered material 11 at the same time the powdered material 11 is being redistributed in the curved channel 32.
Additionally, the powdered material 11 is being moved past the wedge protrusions 60 on the oscillating guide plates 20. This produces a continuous perturbing action that mechanically promotes flow and redistribution of the powdered material 11, therein causing uniformity of the density in the powdered material 11.
Lastly, as the powdered material 11 reaches the end of the curved channel 32, the powdered material 11 is engaged by the agitation tooth 30 on the each of the oscillating guide plates 20. Each agitation tooth 30 cuts into the powdered material 11 and pulls that material either forward or backward relative to the inherent flow of the powdered material 11. This shears the powdered material 11 at its point of thinnest cross-section. agitation tooth. The shearing eliminates clumps and other areas of high density, therein resulting in powdered material 11 that is nearly uniformly dense as it exits the curved channel 32. This uniformly dense powdered material 11 is then fed into the compression Nip zone 14 in between the first roller 16 and the second roller 18. The powdered material 11 is evenly compressed between the first roller 16 and the second roller 18. Since the powdered material 11 is uniformly dense entering the compression zone 14 and the powdered material 11 is uniformly compressed within the compression zone 14, the result is a compressed substrate 12 of uniform, or nearly uniform density.
Different powdered materials have different properties that may require fine adjustments to the powder processing machine 10 in order to operate properly. The articulation rate at which the guide plates 20 move can be selectively controlled by controlling the rotational speed of the eccentric drive shafts 54, 56. The rotational speed of the rollers 16, 18 are controlled as a function of the speed of the auger screw 40. In this manner, the flow of powdered material 11, by weight, into the curved channel 32 is matched to the flow of powdered material 11 entering the compression zone 14. The equal amounts of powdered material 11 entering and exiting the curved channel 32 prevents flow pressure variables from occurring and disrupting the uniform density of the powdered material 11 being processed.
Both the first mounting head 48 and the second mounting head 50 pivot about the eccentric drive shafts 54, 56. As such, each agitation tooth 30 can be deflected by the powdered material 11 passing under the agitation tooth 30. Referring to
The guide pin 72 can be adjustable in position. By adjusting the position of the guide pin 72, the minimum and maximum distance between the agitation tooth 78 and the first roller 79 can be selectively adjusted. In this manner, the oscillating guide plates 70 can be finely adjusted to optimize the processing of different powdered materials. Furthermore, the guide pin 72 can have the form of a camshaft rather than a straight pin. This enables oscillating guide plates 70 of different plate sets to have slightly different movements, therein assisting the oscillating guide plates 70 agitate and shear the powdered material being contacted.
In the previous embodiments, the movement of the various oscillating guide plates is created by rotating eccentric drive shafts. Such a drive mechanism is merely exemplary, and it should be understood that other movement systems can be utilized. For example, the oscillating guide plates can be moved by linkage arms, cams, or any other cyclical drive system. Furthermore, in previous embodiments, multiple oscillating guide plates are used to define the top surface of the curved channel that leads to the compression zone. The use of multiple guide plates is exemplary, and it should be understood that only one guide plate need be used, provided the guide plate is wide enough to fully define the top surface of the curved channel. Referring to
It will be understood that the embodiments of the present invention that are illustrated and described are merely exemplary and that a person skilled in the art can make many variations to those embodiments. All such embodiments are intended to be included within the scope of the present invention as defined by the claims.
This application claims priority rights of the U.S. Provisional Patent Application No. 63/465,085 filed May 9, 2023.
Number | Date | Country | |
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63465085 | May 2023 | US |