The invention relates to an agitating ball mill according to the preamble of claim 1.
Such agitating ball mills have a grinding chamber containing grinding media, a stator and a rotor, which are arranged in the grinding chamber, an input opening and an output opening for feeding and removing grinding material to or from the grinding chamber, as well as a grinding medium separation device arranged in the grinding chamber upstream from the output opening, which is used to separate grinding media entrained in the grinding material from the grinding material before the latter is removed from the grinding space through the output opening.
Agitating ball mills are used in the area of foodstuffs and in the manufacture of fine particles down to the nanometer range in size. Particles or agglomerates suspended in a liquid are here conveyed into the grinding chamber, and comminuted or dispersed in the grinding chamber by means of auxiliary grinding media before being conveyed out of the grinding chamber. To prevent the auxiliary grinding media from becoming dragged out of the agitating ball mill by the liquid stream of grinding material during this wet grinding process, resulting in the loss of the agitating ball mill and contamination of the grinding material, the auxiliary grinding media are held back in the grinding chamber by a separation device. A separating gap, grading screen or cellular wheel are used as separation devices. Essentially spherical elements made out of steel, glass, ceramic or plastic are used as the auxiliary grinding media.
In order to increase the mechanical grinding power introduced into the grinding material in the grinding chamber, the rotor and/or stator of known agitating ball mills is provided with pins that extend into the grinding chamber. As a result, impacts between the grinding material and the pins during operation directly contribute to the grinding power on the one hand. On the other hand, an indirect contribution to grinding power is made by impacts between the pins and the (auxiliary) grinding media entrained in the grinding material and subsequent impacts between the grinding material and grinding media. Finally, the shear and expansion forces acting on the grinding material also help comminute the suspended grinding material particles.
The object of the invention is to achieve an enhanced grinding effect relative to known agitating ball mils at a prescribed rotor/stator geometry or grinding chamber geometry and at a prescribed rotor speed.
The fact that the rotor is essentially shaped like a rotationally symmetric element and the stator is formed by an essentially complementary inner surface of the grinding chamber enables a high power density for the mechanical introduction of energy into the grinding material as well as the greatest possible ratio between the processing area space and processing area volume, and hence an optimal cooling of the grinding material during wet grinding or comminuting.
The fact that the rotor and stator have pins distributed over their entire respective surface, extending from the respective surface and projecting into the processing space enables the direct and indirect action of the pins distributed over the entire grinding chamber volume, i.e., the impacts between the grinding material and pins, the impacts between the pins and the grinding media entrained in the grinding material, as well as the shearing and expansion forces triggered by the pins in the suspension consisting of grinding material and grinding media, which together help comminute the suspended grinding material particles.
As a whole, then, improved grinding power is achieved, accompanied simultaneously by an evening out of grinding intensity, and hence also of an unnecessary strain on the grinding material, e.g., as the result of local overheating, in the entire grinding chamber.
It is particularly advantageous for the grinding material input opening to be arranged in a radially outer area of the grinding chamber, and the grinding material output opening to be arranged in a radially inner area of the grinding chamber. During operation, an equilibrium essentially sets in at on the auxiliary grinding media between a radially outwardly directed centrifugal force component due to the rotation of the rotor around its rotational axis and a radially inwardly directed drag force component due to the grinding material flowing radially from the outside in. The flow of grinding material is maintained by a separate pump, for example. This exposure to centrifugal force provides a “dynamic” relief for the separation device situated radially inside the grinding material output opening, i.e., most of the auxiliary grinding media is suspended, more or less stationary, in the radially outer areas of the processing area, and forms a “swarm” of auxiliary grinding media through which the grinding material is pumped. The few auxiliary grinding media that get into the radially inner area of the processing area in the process are then caught by the separation device. As a result, the separation device is protected and subjected to less wear.
The rotor can essentially be shaped like a truncated cone, wherein the grinding material input opening is arranged in the area of the wide truncated cone end, and the grinding material output opening is arranged in the area of the narrow truncated cone end of the grinding chamber. As an alternative, the rotor can also essentially be shaped like a double truncated cone. In both cases, the grinding material is preferably pumped radially from the outside radially inward.
As a further alternative, the rotor can essentially be shaped like a cylinder, wherein the grinding material input opening is arranged in the area of the first cylinder end, and the grinding material output opening is arranged in the area of the second cylinder end of the grinding chamber, and the grinding material is essentially spirally transported along the cylinder jacket of the rotor through the processing area.
In another advantageous embodiment, the rotor is essentially shaped like a disk, wherein the grinding material input opening is arranged in the radially outer peripheral area, and the grinding material output opening is arranged in the radially inner axial area of the grinding chamber, so that the grinding material again flows through the processing area from the outside in. Here as well, the aforementioned equilibrium between a centrifugal force component and drag force component is also established at the auxiliary grinding media during operation. The grinding material pumped from outside in then once again provides the “dynamic” relief for the radially inner separation device.
It is particularly advantageous for the disk-shaped rotor to have pins on both its two flat disk surfaces and not its peripheral surface. The radially most outwardly lying pins are the fastest of all pins during operation. Since most of the auxiliary grinding media are radially suspended outside, a significant portion of the grinding effect is exerted in just this peripheral area of the processing area alone, resulting in a clearly increase in grinding power at the disk edge by comparison to an agitating ball mill without pins.
The grinding chamber with its stator and rotor and the separation device can preferably be pivoted into a swiveled position in such a way that the separation device arrives at a high location, which is preferably higher than most of the entire grinding chamber volume. This makes it possible to remove the separation device without evacuating the auxiliary grinding medium or product, since the auxiliary grinding medium swell does not reach the height of the separation device in the swiveled position. In addition, this allows the use in the agitating ball mill of a rotatable separation device with spoke or leaf-like elements, e.g., a spoke wheel, paddle wheel or cellular wheel, wherein the separating effect of the separation device only comes about when it starts to rotate. Because the processing zone can swivel according to the invention, the separation device can be made operational in this case, as long as the processing zone is tilted, and the separation device is situated at the high location. After activation, the processing zone is then tilted to the operational setting, in which the auxiliary grinding media now arrive at the separation device, which now exerts a separating action.
Once between 50% and 100% of the entire grinding chamber volume lies under the separation device in the swiveled position, depending on the grinding medium quantity in the agitating ball mill, no auxiliary grinding media will be able to fall out of the grinding chamber owing to the use of a “rotatable” separation device that is inactive when idle, or the lack of a dismantled separation device.
The swiveled, high location of the separation device is best the highest location of the agitating ball mill achievable via swiveling. This facilitates access to the separation device. In addition, auxiliary grinding media located in or on the separation device can be poured out or stripped into the grinding chamber without any problem via the opening to the grinding chamber during the dismantling of the separation device.
The swiveling position is best a non-operating position of the agitating ball mill. In the operating position of the agitating ball mill, the rotational axis of the rotor is essentially arranged horizontally.
The separation device is preferably exchangeable. For example, it can be a self-cleaning grading screen or a paddle wheel.
In another advantageous embodiment, the rotor is a hollow rotor with holes arranged radially inside the rotor, and holes arranged radially outside the rotor. During operation, the auxiliary grinding media are here transported along with a portion of the grinding material flow inside the rotor from a radially inner hole to one of the radially outer holes via the centrifugal action of the rotor, and transported outside the rotor with the entire grinding material flow from the radially outer hole to the radially inner hole via the pumping action of the grinding material input opening, so that the auxiliary grinding media circulate inside the agitating ball mill.
The radially inner hole preferably extends in the circumferential direction given an inner radius Ri at the rotor, and the radially outer hole preferably extends in the circumferential direction given an outer radius Ra at the rotor. This facilitates the entry of auxiliary grinding media along with a portion of the grinding material flow into the rotor cavity, as well as the exit of auxiliary grinding media along with this portion of grinding material flow out of the rotor cavity.
In a particularly preferred embodiment, the hollow rotor exhibits inner channels, which each form a fluid connection between a radially inner hole and a radially outer hole. These spoke-like channels arranged inside the rotor exert a strong centrifugal force on the auxiliary grinding media, so that the latter are transported back out efficiently.
Other advantages, features and possible applications of the invention may be gleaned form the description of an exemplary embodiments based on the drawings, which are not to be construed as limiting.
In addition, the tiltability of the agitating ball mill according to the invention makes it possible to use a separation device other than the “passive” grading screen, e.g., a cellular wheel or a paddle wheel, which can only separate out auxiliary grinding media when operational, i.e., during rotation. If the goal is to stop an agitating ball mill equipped with such an, “active” separation device, it can be tilted in the vertical position with a vertical rotational axis beforehand. The reverse process is followed during renewed startup. The rotor and “active” separation device are first made to rotate with a vertical rotational axis while the agitating ball mill is still tilted, so that the separating action of the “active” separation device is restored, whereupon the agitating ball mill is tilted back into the horizontal operating position with a horizontal rotational axis.
During operation, the product to be ground (e.g., suspension with particles to be comminuted) is pumped via the input opening 11 into the grinding chamber 9, in which the driven rotor disk 21 rotates. The interaction between the grinding media (not shown) and the pins 22, 23 on the rotor disk 21, as well as the pins 24, 25 on the stator, comminutes the particles suspended in the product. The product comminuted and dispersed in this way as it passes through the processing space from the outside in finally arrives at the gap between the grading screen 18 and screen jacket 16, and passes through the grading screen 18 toward the output opening 12. If, despite the high centrifugal field in the grinding chamber 9 and its higher density relative to the grinding material, several grinding media get as far as the grading screen owing to “unfortunate” impacts and/or entrainment by the grinding material flow, they are retained there at the latest. The screen cleaning pins 26 circulating relative to the resting grading screen 18 on its surface with the rotor speed ensure that the grinding material is vigorously swirled with velocity components tangential to the surface of the grading screen. This keeps the grading screen largely free of deposits and conglutinations. In addition, strays are prevented from accumulating among the auxiliary grinding media in the grading screen and quickly jamming the grading screen together with the grinding material.
The disk-shaped rotor marked 21 overall is interspersed by axially parallel pins 22, which are fitted, screwed or otherwise secured in axially parallel boreholes of the rotor disk 21, and project into the grinding chamber from the rotor disk 21 on either of its sides. In addition, pins 23 extending radially out are spaced apart from each other in a circumferential direction on the outer edge of the rotor disk 21. The stator or grinding space casing is formed by the first flat grinding chamber wall 13, the curved grinding chamber wall 14 as well as the second grinding chamber wall 15 (compare
Number | Date | Country | Kind |
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102 40 231 | Aug 2002 | DE | national |
103 13 993 | Mar 2003 | DE | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/CH03/00560 | 8/19/2003 | WO | 00 | 4/21/2005 |
Publishing Document | Publishing Date | Country | Kind |
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WO2004/020098 | 3/11/2004 | WO | A |
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20050211808 A1 | Sep 2005 | US |