This application is the National Stage of PCT/EP2015/053333 filed on Feb. 17, 2015, which claims priority under 35 U.S.C. § 119 of European Application No. 14167217.0 filed on May 6, 2014, the disclosures of which are incorporated by reference. The international application under PCT article 21(2) was not published in English.
The invention relates to an apparatus for accommodation and dispensing of miscible materials, having a cylindrical accommodation vessel having a lower region in the form of a truncated cone, which has a lower discharge opening in the direction of gravity, and having a mixing mechanism shaft disposed centrally in a mixing space, which shaft has at least one mixing mechanism that revolves in the accommodation vessel.
In the state of the art, mixing machines having mixing spaces with rotation symmetry are already known, in which machines the drive shaft of the mixing tools is mounted in the center of the mixing space. A mixer drive having a mixing mechanism shaft with at least one mixing tool is situated in an essentially horizontal pivot axis, wherein the mixing tool is a helical spiral wound around the mixing mechanism shaft in the manner of a helix. According to DE 199 26 045 C2, the mixed material container is a container that narrows in cross-section toward the lower end, with a bottom-side closure for the mixing mechanism. The mechanism dips into the mixed material container when the container is closed. According to DE 198 09 476, the helical spiral is screwed in as it dips into the mixed material. The container according to DE 199 26 045 C2 is self-emptying on the basis of its shaping and the bottom-side closure; mass flow takes place free of de-mixing, in simple manner, quickly, and completely.
The mixing tool is supposed to run through the mixed materials as completely as possible. However, in the case of the apparatuses known in the state of the art, only rotational movement is present in the center of the mixing space. In contrast, rotation and the related translation takes place in the periphery. This also holds true for the mixed materials taken hold of by the mixing tool. They are mixed all the more intensively, the farther they are removed from the axis of rotation of the mixing tool.
A helical-spiral mixing tool generates three-dimensional total flow conditions. In this regard, the upward flow takes place in the periphery, while the downward flow takes place in the center. In order to achieve three-dimensional shifting of the mixed goods, additional mixing mechanisms or complicated mountings are required.
For example, JP 2006 043624 A shows an apparatus for accommodation and dispensing of miscible materials, having a screw that circulates orbitally in the mixing space. A discharge opening is provided in the bottom region of the accommodation vessel, which opening is provided with a bottom lid that is domed upward.
An apparatus for accommodation and dispensing of miscible materials is known from JP S55 76029 U, having a main mixing mechanism disposed centrally in the mixing space and having a spiral-shaped stirring vane, which is disposed along a vessel wall, wherein the discharge opening has a bottom plate that is domed upward.
It is therefore the task of the invention to create a simple solution in which all the mixed materials situated in the mixing space reliably flow through both the zones of slight mixing and the zones of intensive mixing.
This task is accomplished, according to the invention, in that the discharge opening is provided with a displacer apparatus that projects into the interior of the lower region of the accommodation vessel, and that a main mixing tool of the mixing mechanism projects into the approximately V-shaped channel between a lower vessel wall and the displacer apparatus. A displacer apparatus is understood to be not only a dynamic element but also a static element.
In this way, it is ensured that all of the particles involved in a formulation come into relative motion with regard to the adjacent particles, in each instance. The displacer apparatus guides the mixed materials from the center of the mixing space into its periphery. There, they are taken up by the main mixing tool, i.e. by the lower end of the mixing screw or mixing spiral of the mixing mechanism, which projects into the channel that is between lower vessel wall and the displacer apparatus and that is approximately V-shaped in cross-section, and conveyed upward. As a result, perfect flow conditions of the mixed material take place even in the conical bottom region of the mixing space, in more space-controlling and effective manner. At the same time, low-wear mixing is possible, the mixing space can be. cleaned perfectly after being emptied and, at the same time, it forms a mixing container as well as a reactor container.
In this way, it is possible to mix even components having different flow suitability values, densities, degrees of moisture, and particle sizes with one another in reliable and uniform manner. At the same time, the apparatus can optionally be operated as a batch mixer or a continuous mixer.
At the same time, the known problems of upright-standing mixers having a vertically mounted mixing mechanism shaft are solved. Usually, the mixed materials lie all the more heavily one on top of the other; the dynamic pressure in the lower mixer region increases in proportion to how large the mixer is configured to be. In such a case, the mixed materials can easily become compacted and form clumps. The mixing tool then has to overcome the increased dynamic pressure. The mixing process is made more difficult because loosening effects are absent. This happens particularly frequently if the bottom of the vertical mixer has a cone or truncated cone. The materials situated in the lower mixer region, which narrows conically, can practically not be loosened because of the circulating circumference speed of the mixing tool, and therefore they cannot flow freely. For this reason, the materials situated here move almost only in a circle. Until now, attempts were made to optimize the spiral shape of the mixing tool and to increase the speed of rotation. However, this is only possible to a limited extent in the case of large mixers. In every case, the mixing time must be drastically lengthened. In some cases, part of the mixed material is actually removed from the mixing vessel at the bottom, during mixing, and put back into the mixing space from above.
All of these difficulties are eliminated by the new solution according to the invention, in which the mixed material is guided from, the center into the periphery by the displacer apparatus that projects into the lower region of the accommodation vessel, where the material is taken up by the lower end of the mixing screw or mixing spiral of the mixing mechanism, which end projects into the channel between lower vessel wall and displacer apparatus, which channel is approximately V-shaped in cross-section, and conveyed upward by the helical spiral that is wound around the mixing mechanism shaft in helix shape, with the corresponding translation movement, before it trickles down or flows down again from there along the mixing mechanism shaft in the center of the mixing mechanism.
It is advantageous if the displacer apparatus can be pushed into the interior of the accommodation vessel to open the discharge opening, and, for this purpose, it is advantageous if it is disposed within the mixing space. In this regard, the displacer apparatus is suitable for dipping into the mixing space, in order to empty the vessel, which is open at the bottom, and the mixer, without colliding with the mixing tool and without impairing the mixing efficiency.
Alternatively, the displacer apparatus can also be lowered below the discharge opening to open the discharge opening, also without colliding with the mixing tool and without influencing the mixing efficiency.
It is practical if the displacer apparatus has a greater diameter at its lower edge than the discharge opening of the mixing vessel, if it is disposed within the mixing space and can be pushed into the interior of the accommodation vessel to open the discharge opening. In this way, tight and secure closure of the emptying opening is ensured. The same holds true if the displacer apparatus can be lowered below the discharge opening to open the discharge opening. In this regard, the displacer apparatus can be moved translationally into the mixing space or can be lowered out of it. Alternatively, it can be moved into the lower region of the accommodation vessel or lowered out of it by means of a lifting/rotating movement.
In every case, it is provided that the displacer apparatus ends with the lower vessel wall, in sealed manner. The displacer apparatus can be formed to be conical, hyperbola-like, parabola-like, scale-like, dome-like, roof-like, hemispherical, trumpet-shaped, droplet-shaped, in the form of a truncated cone, convex or concave. Likewise, a static, smooth or dome-like configuration is possible. The displacer apparatus can be structured as a component fixed in place. It can also be driven and mounted on the underside, and can be designed in both high-speed and low-speed manner. The displacer apparatus can be configured to be convex or concave. It can furthermore be translationally moved into the mixing space or lowered out of it. Furthermore, the displacer apparatus can be structured as an opening.
Further embodiments are evident from the dependent claims. In particular, multiple, particularly two or three accommodation vessels can also overlap with one another, in such a manner that a two-shaft or three-shaft mixer, having further improved mixing properties, can be formed.
It is particularly advantageous if the displacer apparatus is formed and composed in such a manner that the miscible materials slide along it due to gravity. In this way, the miscible materials or the mixed material get from the center of the mixing space into its periphery, and thereby into the acquisition range of the mixing tools, in simple manner.
It is furthermore advantageous if the main mixing tool is shaped in such a manner that it takes up the mixed material even at the bottom of the channel that is approximately V-shaped in cross-section. In this way, acquisition without a dead space and reliable mixing of the mixed goods are achieved.
The mixed material can easily be conveyed upward along the lower vessel wall, out of the channel that is approximately V-shaped in cross-section, and effectively mixed, using a main mixing tool that is adapted to the contour of the lower vessel wall.
A significant advantage furthermore results from the fact that the main mixing tool is shaped to be contour-parallel, corresponding to the lower vessel wall. Thus, the main mixing tool is adapted to the contour of the lower vessel wall in such a manner, in this case, that a preferably uniform small gap between main mixing tool and lower vessel wall exists over the tool length. In this way, particularly effective mixing can be achieved.
It is particularly advantageous if a clearance angle is disposed between the lower vessel wall and the main mixing tool. In this way, it can be ensured that the mixed material that gets between the lower vessel wall and the formed-on main mixing tool is not stressed, in other words not subjected to further strain or loads.
It is furthermore advantageous that the displacer apparatus is stripped off by the main mixing tool in certain regions. If this region is provided in a lower region part of the displacer apparatus, and if this region part extends all the way to the bottom of the channel that is approximately V-shaped in cross-section, particularly good mixing of the mixed materials is guaranteed. Preferably, the stripped-off lower region part should maximally amount to one-third of the total height of the displacer apparatus that projects into the interior of the lower region of the accommodation vessel.
A further advantageous embodiment provides that the incline of the surface between a lower edge of the displacer apparatus and an upper end of the displacer apparatus has an angle of at most 65 degrees relative to the direction of gravity after the lifting/rotating movement. This means that the incline of the surface with which the displacer apparatus projects into the lower region of the accommodation vessel amounts to about 25 degrees or more relative to a horizontal plane that lies orthogonal to the direction of gravity, even in the open position. What is advantageous about this embodiment is that the displacer apparatus does not have to be lowered completely out of the mixing space. Thus, dispensing of the miscible materials through the discharge opening, in the direction of gravity, already takes place at slight opening angles of 15 to 30 degrees. Thus, even a slight lifting/rotating movement already suffices to open the discharge opening to such an extent that the miscible materials are dispensed through the discharge opening due to gravity. This measure therefore saves costly construction space below the discharge opening.
Further characteristics, details, and advantages of the invention are evident on the basis of the following description and using the drawings. Some exemplary embodiments of the invention are explained in greater detail, as examples, using the following drawings. Objects or elements that correspond to one another are provided with the same reference symbols in all the figures. These show:
An apparatus for accommodation and dispensing of miscible materials, according to the invention, indicated in general with 1, has an essentially cylindrical accommodation vessel 2 having a lower region 3 in the form of a truncated cone, with a lower discharge opening 4 in the direction of gravity, and with a mixing mechanism 5 that circulates in the accommodation vessel 2. The mixing space 7 of the apparatus 1 according to the invention is formed by the accommodation vessel 2 and the lower region 3 in the form of a truncated cone. The circulating mixing mechanism 5 with its additional mixing tools 5′, 5″ is disposed in this mixing space 7. The mixing mechanism shaft 6 of the mixing mechanism 5, which also serves as a drive shaft for the mixing tools 5′, 5″, is mounted centrally in the mixing space 7. A mixer drive, not shown in any detail, is situated above on an essentially horizontal pivot axis. The mixing mechanism shaft 6 has at least one mixing mechanism 5 that can also be wound around the mixing mechanism shaft 6 in helix manner, as a helical spiral. A further mixing tool 9 can be disposed at the lower, tapered free tip 8 of the mixing mechanism shaft 6, as the main mixing tool.
According to the invention, the discharge opening 4 is provided with a displacer apparatus 10 that projects into the interior of the lower region 3, in the form of a truncated cone, of the accommodation vessel 2. This apparatus can particularly be structured as a closure cone with an acute angle or a wide angle. Its shape can be structured, for example, to be conical, hyperbola-like, parabola-like, scale-like, dome-like, roof-like, hemispherical, trumpet-shaped, droplet-shaped, in the form of a truncated cone, convex or concave. It is also possible to configure the displacer dynamically, for example approximately in sickle shape 10a, as shown, for example, in
It is provided, in every case, that the displacer apparatus 10, 10a ends by contacting and sealing the lower edge 11 of the vessel wall 13, forming a seal at a circumferential sealing region. It can also be translationally movable into the mixing space 7 or can be lowered out of it.
The displacer apparatus 10 can be structured as a fixed component, on the one hand, but it can also rotate as shown with the reference symbol 10a in
In every case, it is advantageous if the displacer apparatus 10 is shaped, following the conical wall part of the lower vessel wall 13, in such a manner that the rotating main mixing tool 5″ or 9 can take up the mixed material free of dead space, and in stress-free manner. The Lower vessel wall 13 and the cylindrical accommodation vessel 2 can also have a surface having a hydrophobic nanostructure.
In an embodiment, it is provided that the displacer apparatus 10 is stripped off by the rotating main mixing tool 5″. Furthermore, a mixing tool 14 can additionally be disposed on the displacer apparatus 10, as is evident from
The significant advantage of the apparatus according to the invention consists in that the mixed material, which essentially flows down in the center, along the mixing mechanism shaft 6, which serves as the drive shaft of the mixing tools 5′, 5″, is guided, at the bottom of the accommodation vessel 2, which ends in the shape of a truncated cone, by the mixing mechanism shaft 6, in other words the axle of rotation of the mixing mechanism 5, to the periphery, where upward flow takes place. As a result, all the mixed materials situated in the mixing space 7 can reliably flow through both the zones of slight mixing and the zones of intensive mixing. This is guaranteed in that the main mixing tool 5″, in other words the lower end of the mixing screw or the lowermost element of the mixing mechanism 5, projects into the approximately V-shaped channel 16 between lower vessel wall 13 and displacer apparatus 10. In this regard, the displacer apparatus 10 can be both a dynamic element 10a and a static element 10. In every case, it is ensured that all the particles participating in the formulation come into relative motion with regard to the adjacent particles, in each instance. The problems that have existed until now in the case of vertical mixers having a conical outlet or an outlet in the form of a truncated cone, which problems consist in that the materials situated in the center practically only turn in a circle, are solved in simple and effective manner.
The accommodation apparatus 1 can be simply opened and emptied in the manner described, specifically without residue. This can be done either in that the displacer apparatus 10 is lowered below the discharge opening 4 or displaced info the interior of the accommodation vessel 2, specifically either by means of a translational movement or a lifting/rotating movement. Alternatively, it is provided that the displacer apparatus 10 can be flexibly inflated or shrunken, as shown in
Particular advantages occur if two apparatuses 1, 1′, 1″ according to the invention are combined with one another, as shown in
A further cross-section through the lower region 3 of the accommodation vessel 1 (
The detail in
In the detail in
In the detail of
In the detail of
In the detail in
In the detail of
In the detail of
Of course, the invention is not restricted to the exemplary embodiments shown. Further embodiments are possible without departing from the basic idea. Thus, it is also possible, for example, to configure the displacer apparatus 10 dynamically, not statically. In this case, a displacer apparatus 10a rotates about its own axis 19, as shown in
Number | Date | Country | Kind |
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14167217 | May 2014 | EP | regional |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2015/053333 | 2/17/2015 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
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WO2015/169458 | 11/12/2015 | WO | A |
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Entry |
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International Search Report of PCT/EP2015/053333, dated Jun. 1, 2015. |
Number | Date | Country | |
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20160354743 A1 | Dec 2016 | US |