A rotary blade or impeller for mixing fluent, particulate, slurry, semi-liquid, or liquid materials is disclosed. More particularly, a rotary impeller is disclosed that is specifically adapted for mixing materials that contain agglomerates or other clumped masses of a type that necessarily requires relatively high shear and cutting action to enable grinding and breaking apart of the agglomerates and dissemination and dispersion thereof within a mixture.
Rotary impellers are known for use in a wide variety of industrial mixing applications to mix particulate materials, slurries and the like having various characteristics by creating turbulent flow of fluent material within a vessel when the impeller is rotated by a rotatable shaft of a mixing apparatus. Rotary impellers may also be used in an attempt to finely grind and break apart solid materials and/or agglomerates of materials that may or may not be suspended within a carrier material or fluid and to evenly disperse the solid material or agglomerates within the carrier material. Typically, the ability of the impeller to finely grind solid particles or agglomerates to a desired reduced size and to evenly disperse these particles throughout the carrier material is important toward the effectiveness of a final mixture. Thus, failure to provide a homogeneous final mixture can compromise the integrity of the product formed by the mixture and may prevent the product from functioning properly. Impeller imparts shear and collisions of particles causing particles to break apart.
Some mixing applications include grinding of particulate materials, powders, or slurries containing agglomerates that are particularly difficult to break apart and reduce in size and evenly disperse within a material. Such materials may include, for instance, high viscosity slurries and carrier materials having relatively hard and dense agglomerates and solid particles suspended therein. A blade or impeller for applications involving such materials is desired.
An impeller is provided which, in use, is disposed and mounted on a rotating shaft of mixing apparatus and immersed within a material to be subject to mixing and/or grinding. According to an embodiment, the impeller has a substantially disk-shaped body with a generally-circular outer diameter. The body has a thickness, opposite major faces, a peripheral side face, and a central bore. The thickness of the body is essentially constant and uniform and the major faces are essentially planar, except for the existence of a series of grooves and teeth discussed in detail below.
Several, separate, radially-extending, spaced-apart grooves or so-called “scoops” are formed in one or both of the major faces of the disk-shaped body such that the grooves or scoops extend through and appear in the outer peripheral side edge or face of the body. The grooves or scoops may be provided in the form of shallow recesses that do not extend through the full thickness of the disk-shaped body. Thus, at the locations of the grooves, recesses, or scoops, the thickness of the disk-shaped body is reduced as compared to other locations. By way of example, each groove may only extend through approximately half the full thickness of the disk-shaped body. Of course, each groove could extend through more or less of the full thickness of the body provided not entirely through the full thickness of the body.
Each groove may have a curved profile in transverse cross-section, such as when viewed from the side edge or face of the disk-shaped body. When grooves are formed in both major faces of the body, the same number and size of grooves may be provided on both major faces such that both major faces are of a substantially identical configuration. However, the grooves formed in one of the major faces may be circumferentially offset with respect to the grooves formed in the opposite major face such that, upon viewing the body from the side edge or face, a groove on one major face may be spaced between two adjacent grooves on the opposite major face.
According to an embodiment, the impeller is specifically adapted to mix and break-up settled powder and grind difficult to disperse agglomerates that may require both high shear and cutting action for proper agglomerate size reduction and even dispersion of the agglomerates within a mixture. For this purpose, the impeller includes a plurality of separate tooth-like protrusions projecting outward from one or both of the major faces of the body. The protrusions may be located adjacent the outer diameter of the disk-shaped body and be circumferentially-spaced apart along the outer edge thereby aiding in defining the surface shape and appearance of the side edge or face of the body. The protrusions may also be located at locations spaced from the outer diameter of the body.
When the disk-shaped impeller body is rotated, the set of teeth or projections work in concert with the grooves, recesses, or scoops to finely grind solid material, particles, and agglomerates and improve turbulent flow of the material being mixed. This ultimately improves the efficiency of finely grinding, breaking up, and evenly dispersing the solid particles and agglomerates within the mixture. In particular, the teeth are provided to create an aggressive cutting action during vortex formation of the carrier material, slurry, or fluid. The teeth also enable the size of powder type materials and agglomerates to be greatly reduced as compared to other impeller configurations and designs.
Further, the number and size of teeth on the disk-shaped impeller body can be provided for temperature control purposes such that, as the impeller body is rotated, the set of teeth or projections enable the amount of heat generated within a batch of material being mixed to be precisely controlled. For instance, the more teeth added to the impeller body, the greater the heat generated within a material being mixed as a result of greater energy input. Embodiments of the impeller blade have been found to be able to run significantly cooler batches as compared to when a conventional steel blade is utilized. Also, embodiments of the impeller blade have been found to build heat within a batch of material being mixed much quicker than conventional impellers. In this manner, the number of teeth can be particular selected based on the particular temperature control needs of an end user depending upon whether the end user seeks the impeller blade to run relatively hot or cold with respect to the generation of heat within a batch of a material being mixed.
The number of teeth and/or scoops on a face of the disk-shaped body may be varied depending upon the material being ground, broken apart, and dispersed. The placement of the teeth and/or scoops on the face of the disk-shaped body may also be varied and may be provided on only one of the faces or both of the faces of the disk-shaped impeller body. In use, the impeller may be used alone as a single mixing blade or may be used with other like impellers mounted in a series above or below each other or next or adjacent to each other within a mixing vessel.
The impeller body may be made from polymers, metal, ceramics or other materials. According to one example of an embodiment, the impeller body is molded or fabricated such that the teeth are integrally formed on the impeller body. For example, the impeller body, including the teeth, may be molded of urethane, polyurethane, polyethylene, Ultra High Molecular Weight (UHMW) polyethylene, Polytetrafluoroethylene (PTFE), polypropylene, nylon, or the like. According to another embodiment, the impeller body may include a dynamically balanced metal plate embedded therein, such as a steel plate. As yet another alternative, the impeller body may be fabricated of a ceramic or metallic material.
The impeller body having the teeth and scoops discussed above may be mounted on a rotating shaft of a mixing machine by a wide variety of means including keyways, bolt holes, hubs and couplings.
One contemplated embodiment of an impeller body 10, referenced as a first embodiment herein, is shown in
The impeller body 10 may be disc shaped having a central bore about which a separately manufactured hub 26 may be secured. The disc-shaped impeller body 10 includes an outer peripheral side edge face 12 defined by a predetermined outer diameter of the body 10. The dimension of the outer diameter may be provided based on the mixing apparatus or material to be mixed. By way of example, the outer diameter of the impeller body 10 may be, for instance, between 3 inches and 32 inches. As a specific example, the body may have an outer diameter of 7, 8 or 9 inches. However, one of ordinary skill in the art will appreciate that the impeller body may be of any diameter and may even be produced of non-circular configurations as may be required for a particular application.
As shown in
The grooves 14 and 18 are each evenly spaced apart about the circumference of the body 10 and are located adjacent the outer-peripheral side edge face 12. The grooves 14 on the face 16 and the grooves 18 on the opposing face 20 are circumferentially offset such that the grooves on one face are equally spaced between the grooves on the other face and are not directly opposed. In addition, the grooves 14 and 18 are provided in the form of recesses that do not extend through the entire thickness of the body 10, but do extend into the outer peripheral side edge face 12. For instance, see
In the first embodiment as shown in
There may be any number of grooves per face including even or odd grooves per face. For instance, in
The impeller body 10 shown in
Simply for purposes of example, each groove and teeth pairing may include two separate teeth spaced apart by the width of the groove. In other contemplated embodiments, there may be more or less teeth and more or less grooves and the spacing therebetween may differ. In the embodiment illustrated in
In the first embodiment, the width of each tooth is generally half the width of each groove, and the spacing between teeth that are not separated by a groove along the outer peripheral side edge face 12 of the body 10 is about the same as the width of each tooth. Thus, each tooth is separate and individual and does not contact other teeth or extend within a groove. Some contemplated embodiments may not utilize the above relationships between tooth and groove sizing and spacing.
In the first embodiment, the height of each of the teeth is generally slightly greater than the thickness of the body 10 where no groove is located, and each of the teeth extends along approximately one-fourth of the length of each groove. As stated above, some contemplated embodiments may not utilize the above relationships with respect to the height and length of each tooth relative to the depth and length of each groove. For example, the shape and size of the teeth may be selected based on the viscosity or type of solid particles or agglomerates to be subject to mixing. For example, a greater number and size of teeth may be used for more viscous fluids and/or more abrasive particles or agglomerates having properties making them more difficult to grind.
Merely for purposes of example, each tooth may have a substantially box-like configuration having a planar top surface 30 with four corners closely resembling a rectangle, for instance, as shown in
In the first embodiment, one of the vertical sides 32 of each tooth forms a surface of the outer peripheral edge face 12; thus, this vertical side 32 of the tooth is necessarily slightly arcuate following the contour dictated by the outer diameter of the disk-shaped body 10. The opposite or inner vertical side 34 of each tooth is also formed along a diameter that is spaced inward of the outer diameter. As an alternative, the sides of the teeth may be formed irrespective of the outer diameter. The length of each tooth between the outer vertical side 32 and opposite inner vertical side 34 may be substantially constant and uniform. The end vertical side faces 36 of each tooth may be planar and parallel to each other. Thus, each tooth may define four sharp vertically-extending corner edges extending from the body 10 to the planar top surface 30. However, as stated above, the shape of the teeth may be varied and include a rounded top and/or rounded corners.
A second embodiment of an impeller body 40 is shown in
As shown in
In the second embodiment as shown in
The impeller body 40 has six grooves 44 and 48 on each major face, 46 and 50. However, this merely provides an example of one contemplated embodiment and other embodiments may have more or less grooves. The impeller body 40 includes a plurality of teeth 52 projecting from the major face 46 and a plurality of teeth 54 projecting from the major face 50. Each of the teeth 52 and 54 is provided by a solid outward projection formed along and adjacent the outer peripheral side edge face 42 of the body 40. The teeth 52 and 54 may be a uniform size and shape. As shown in
In the second embodiment, the width of each tooth is generally half the width of each groove, and the spacing between teeth that are not separated by a groove along the outer peripheral side edge face 42 of the body 40 is about the same as the width of each tooth. Thus, each tooth is separate and individual and does not contact other teeth or extend within a groove. Each of the teeth extends along approximately one-half of the length of each groove and may have a substantially trapezoidal configuration in plan view.
As shown in
In the third embodiment as shown in
Body 60 has six grooves 64 and 68 on each major face, 66 and 70, and includes a plurality of teeth 72 projecting from the major face 66 and a plurality of teeth 74 projecting from the major face 70. Each of the teeth 72 and 74 is provided by a solid outward projection formed along and adjacent the outer peripheral side edge face 62 of the body 60. The teeth 72 and 74 may be a uniform size and shape. As shown in
In the third embodiment, the spacing between teeth that are not separated by a groove along the outer peripheral side edge face 62 of the body 60 is less than (about half) the width of each tooth. Thus, each tooth is separate and individual and does not contact other teeth or extend within a groove. The teeth extend along approximately one-half of the length of each groove. Merely for purposes of example, each tooth 52 and 54 of the second embodiment may have a substantially trapezoidal configuration in plan view.
The impeller bodies 10, 40 and 60 provide examples of embodiments in which the teeth are molded or fabricated integral with the impeller body and are made of the same material as the impeller body. For instance, the body including the teeth may be molded or fabricated of polyurethane. In use, the teeth are provided to break apart and disperse solid particles or agglomerates and alter turbulent flow so as to maximize particle dispersion.
The surface, shape, and appearance of the outer peripheral side face or edge 12, 42 and 62 of the impeller bodies 10, 40 and 60 are best shown in
The arched-shaped openings or channels 80 are defined by a groove and teeth on adjacent sides of the groove. The opening or channel may have a consistent and uniform size along the length of each of the teeth defining the channel. Thus, the opposed vertical end side faces of each pair of teeth that are separated by a groove may be parallel. In contrast, the smaller openings 82 are formed between each pair of adjacent teeth that are not separated by a groove. The opposed vertical end faces of such teeth are not parallel and therefore may converge toward each other (see
A mounting structure used to mount the impeller bodies to a rotatable shaft (not shown) may include a hub (for instance, hub 26) comprising an annular metal collar 84 secured to the impeller body and extending through the center bore of the impeller body. In use, the collar 84 enables the body to be connected to a rotatable shaft of a mixing machine (not shown) such that the impeller body rotates when the shaft rotates. As shown in
When the impeller configurations discussed above are immersed within a fluent material in a vessel and rotated, the motion of the impeller sets up a vibration around the periphery of the impeller body. The alternating configurations of the grooves on the opposite faces of the impeller body induces an up and down motion of the fluent material around the periphery of the impeller, thereby, establishing a vortex. The teeth and configuration thereof and of the differently shaped channels on the edge of the impeller provide high shear and cutting action sufficient to break agglomerates and finely grind solid particles within the fluent material or slurry and alter the turbulent flow produced by the grooves.
Variations of the above described embodiments may be made without departing from the scope of the invention as defined in the appended claims.
This application claims the benefit under 35 USC §119(e) of U.S. Provisional Patent Application No. 62/032,712 filed Aug. 4, 2014.
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Number | Date | Country | |
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Number | Date | Country | |
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62032712 | Aug 2014 | US |