CN215540452U - Production system is ground to compounding - Google Patents
Production system is ground to compounding Download PDFInfo
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- CN215540452U CN215540452U CN202121325223.7U CN202121325223U CN215540452U CN 215540452 U CN215540452 U CN 215540452U CN 202121325223 U CN202121325223 U CN 202121325223U CN 215540452 U CN215540452 U CN 215540452U
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Abstract
The utility model discloses a mixed material grinding production system which comprises a coarse grinding subsystem, a fine grinding subsystem and at least two groups of mixed material subsystems. The material mixing subsystems are connected in parallel. The coarse grinding subsystem comprises at least two coarse grinding tanks connected in parallel and at least two coarse grinders connected in parallel; the rough grinding tank is connected to one end and then connected with the rough grinding machine; the mixing subsystem is connected with one end and then connected with the rough grinding subsystem. The fine grinding subsystem comprises at least two fine grinding tanks connected in parallel and at least two fine grinders connected in parallel; the fine grinding tank is connected to one end and then connected with the fine grinding machine; the coarse grinding tank and the coarse grinding machine are connected to one end and then connected with the fine grinding subsystem. When a certain node or a certain device on the production system goes wrong, the production system can continue to produce through other channels, the whole production line does not need to be stopped, continuous production can be realized, and the production efficiency is high.
Description
Technical Field
The utility model relates to the technical field of mixed material grinding, in particular to a mixed material grinding production system.
Background
The mixing and grinding process is two processes often involved in various production lines. The mixing process can mix various raw materials for subsequent production. Grinding is to grind and crush the raw materials so that the granularity of the raw materials is smaller.
At present, most of mixed material grinding production systems can use a single-group series arrangement mode, and various devices in the production systems are arranged in a single-line communication mode. According to the arrangement mode, the production route is only a single channel, once a certain node or a certain device on the production system goes wrong, the whole production system can only stop running, and can only be operated again after the problems are solved, so that the continuous production is not facilitated, and the production efficiency is low.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a mixing and grinding production system which is beneficial to continuous production and high in production efficiency.
The utility model discloses a mixed material grinding production system which comprises a coarse grinding subsystem, a fine grinding subsystem and at least two groups of mixed material subsystems. The material mixing subsystems are connected in parallel. The coarse grinding subsystem comprises at least two coarse grinding tanks connected in parallel and at least two coarse grinders connected in parallel; the rough grinding tank is connected to one end and then connected with the rough grinding machine; the mixing subsystem is connected with one end and then connected with the rough grinding subsystem. The fine grinding subsystem comprises at least two fine grinding tanks connected in parallel and at least two fine grinders connected in parallel; the fine grinding tank is connected to one end and then connected with the fine grinding machine; the coarse grinding tank and the coarse grinding machine are connected to one end and then connected with the fine grinding subsystem.
Optionally, at least two groups of fine grinding subsystems are arranged, and the coarse grinding tank and the coarse grinding machine are connected to one end and then connected with each group of fine grinding subsystems.
Optionally, the production system includes at least two sets of feeding subsystems, and each set of feeding subsystem is connected with the mixing subsystem.
Optionally, the production system includes at least two finished product tanks, and the fine grinding tank and the fine grinding machine are connected to one end and then respectively connected to the finished product tanks.
Optionally, the mixing subsystem comprises a dosing tank and a homogenizing pump; the batching tank and the homogenizing pump are connected and form a circulation loop.
Optionally, the feeding subsystem comprises a feeding bin and a metering bin, the feeding bin is connected with the metering bin, and the metering bin is connected with the mixing subsystem.
Optionally, the mixing subsystem comprises a filter; the filter is arranged between the dosing tank and the homogenizing pump.
Optionally, the rough grinding subsystem comprises a first heat exchanger and a first diaphragm pump; the first heat exchanger and the first diaphragm pump are arranged before the rough grinding machine.
Optionally, the fine grinding subsystem comprises a second heat exchanger and a second diaphragm pump; the second heat exchanger and the second diaphragm pump are arranged before the rough mill.
Optionally, a delivery pump is arranged between the coarse grinding subsystem and the fine grinding subsystem, and between the fine grinding subsystem and the finished product tank.
According to the mixed material grinding production system, the mixed material subsystem is arranged in parallel, the coarse grinding tanks connected in parallel and the coarse grinding mills connected in parallel are arranged in the coarse grinding subsystem, the fine grinding tanks connected in parallel and the fine grinding mills connected in parallel are arranged in the fine grinding subsystem, and the production system forms a multi-channel production route.
Drawings
The accompanying drawings, which are included to provide a further understanding of the embodiments of the utility model and are incorporated in and constitute a part of this specification, illustrate embodiments of the utility model and together with the description serve to explain the principles of the utility model. It is obvious that the drawings in the following description are only some embodiments of the utility model, and that for a person skilled in the art, other drawings can be derived from them without inventive effort. In the drawings:
FIG. 1 is a schematic diagram of a compounding mill production system according to an embodiment of the present invention;
FIG. 2 is a schematic diagram of a compounding subsystem according to an embodiment of the present invention;
FIG. 3 is a schematic diagram of a rough grinding subsystem in accordance with an embodiment of the present invention;
FIG. 4 is a schematic view of a fine grinding subsystem in accordance with an embodiment of the present invention;
FIG. 5 is a schematic diagram of a feed subsystem according to an embodiment of the present invention;
fig. 6 is a schematic view of a finished can of an embodiment of the present invention.
100, a mixing subsystem; 110. a dosing tank; 120. a homogenizing pump; 130. a filter; 200. a coarse grinding subsystem; 210. a coarse grinding tank; 220. a rough grinding machine; 230. a first heat exchanger; 240. a first diaphragm pump; 300. a fine grinding subsystem; 310. finely grinding the tank; 320. a fine grinding machine; 330. a second heat exchanger; 340. a second diaphragm pump; 400. a feed subsystem; 410. a feeding bin; 420. a metering bin; 500. a finished product tank; 600. a delivery pump; 700. a pipeline.
Detailed Description
It is to be understood that the terminology, the specific structural and functional details disclosed herein are for the purpose of describing particular embodiments only, and are representative, but that the present invention may be embodied in many alternate forms and should not be construed as limited to only the embodiments set forth herein.
The utility model is described in detail below with reference to the figures and alternative embodiments.
As shown in fig. 1, as an embodiment of the present invention, a compounding grinding production system is disclosed, which includes a coarse grinding subsystem 200, a fine grinding subsystem 300, and at least two compounding subsystems 100. The mixing subsystems 100 are connected in parallel. The coarse grinding subsystem 200 includes at least two coarse grinding tanks 210 connected in parallel and at least two coarse grinders 220 connected in parallel; the rough grinding tank 210 is connected to one end and then connected to the rough grinding machine 220; the blending subsystem 100 is connected to one end and then connected to the rough grinding subsystem 200. The fine grinding subsystem 300 includes at least two fine grinding tanks 310 connected in parallel and at least two fine grinders 320 connected in parallel; the fine grinding tank 310 is connected to one end and then connected with the fine grinding machine 320; the rough grinding tank 210 and the rough grinding mill 220 are connected to one end and then connected to the fine grinding subsystem 300.
The mixing subsystem 100 is used for uniformly mixing various raw materials for use in subsequent processes. The coarse grinding subsystem 200 performs a preliminary grinding of the raw material and further grinds the raw material through the fine grinding subsystem 300 to obtain finer raw material. Wherein the rough grinding tank 210 of the rough grinding subsystem 200 is used for storing raw materials, and the rough grinding machine 220 performs a preliminary grinding on the raw materials. After the primary grinding by the coarse grinding subsystem 200, the raw material is delivered to the fine grinding subsystem 300. Wherein the fine grinding tank 310 of the fine grinding subsystem 300 is used for storing raw materials, and the fine grinder 320 further grinds the raw materials to obtain finer raw materials.
According to the mixing grinding production system, the mixing subsystem 100 connected in parallel, the rough grinding tanks 210 connected in parallel and the rough grinding mills 220 connected in parallel in the rough grinding subsystem 200 are arranged, the fine grinding tanks 310 connected in parallel and the fine grinding mills 320 connected in parallel in the fine grinding subsystem 300 are arranged, and the production system forms a multi-channel production line.
For example, when one of the compounding subsystems 100 has a problem, the compounding subsystem 100 having the problem may be shut down, and the remaining compounding subsystems 100 may continue to produce without being affected. For another example, when one of the rough mills 220 is used, the rough mill 220 with a problem can be shut down, the rest of the rough mills 220 can continue to produce without being affected, the operation of the whole mixed material grinding production system is not affected, continuous production can be realized, and the production efficiency is high.
Wherein the compounding subsystem 100 can be two, three, four, or even more. Each group is connected in parallel. For example, when the mixing subsystems 100 are three groups, the three groups of mixing subsystems 100 are arranged in parallel to form three channels, and each group of mixing subsystems 100 performs mixing operation. Any one group or even two groups of the mixing subsystem 100 have problems, and the mixing grinding production system can also normally carry out production, so that the aim of repairing and producing at the same time can be fulfilled.
Wherein, the number of the rough grinding tanks 210 and the rough grinding mills 220 can be two, three, four, or even more. Each rough grinding tank 210 is connected in parallel, and all the rough grinding tanks 210 are connected to one end and then connected to the rough grinding mill 220. The coarse grinding machines 220 are connected in parallel. For example, when there are three coarse grinding machines 220, three coarse grinding machines 220 are arranged in parallel, and each group of coarse grinding machines 220 is in grinding operation. Any one of the rough mills 220, even two of the rough mills are in trouble, and the mixed material grinding production system can also normally carry out production, so that the aim of repairing and producing at the same time can be fulfilled. The number of the rough grinding tank 210 and the rough grinding machine 220 may be the same or different, and may be specifically set according to the requirement.
Wherein, the fine grinding tank 310 and the fine grinding machine 320 can be two, three, four or even more. Each of the fine grinding tanks 310 is connected in parallel, and all the fine grinding tanks 310 are connected to one end and then connected to the fine grinding machine 320. The fine mills 320 are connected in parallel. For example, when there are three said fine mills 320, three said fine mills 320 are arranged in parallel, and each said fine mill 320 is in grinding operation. When any one or even two of the fine mills 320 have problems, the mixed material grinding production system can also normally carry out production, and the purpose of repairing and producing can be realized. In terms of number, the number of the fine grinding tank 310 and the number of the fine grinding machine 320 may be the same or different, and may be specifically set according to needs. The rough mill 220 and the fine mill 320 may be sand mills or the like.
Specifically, as shown in fig. 2, the compounding subsystem 100 includes a batching tank 110 and a homogenizing pump 120; the batching tank 110 and the homogenizing pump 120 are connected and form a circulation loop. The batching tank 110 is used for storing raw materials and the homogenizing pump 120 is used for homogenizing raw materials. In the present embodiment, the material blending tank 110 and the homogenizing pump 120 are connected to form a circulation loop, and the raw material in the material blending tank 110 may be circulated back to the material blending tank 110 after being homogenized by the homogenizing pump 120, and then may continue to be circulated and homogenized until the homogenization is completed. The raw material is then delivered to the fine grinding subsystem 300.
Specifically, the compounding subsystem 100 includes a filter 130; the filter 130 is disposed between the batching tank 110 and the homogenizing pump 120. The raw material is filtered by the filter 130 before entering the homogenizing pump 120 from the batching tank 110, preventing the raw material from clogging the homogenizing pump 120 during the homogenization process. After the raw materials are processed in the blending subsystem 100, the raw materials are transported to the rough grinding subsystem 200 for preliminary grinding.
As shown in fig. 3, the coarse grinding subsystem 200 includes a first heat exchanger 230 and a first diaphragm pump 240; the first heat exchanger 230 and the first diaphragm pump 240 are disposed before the rough mill 220. The first heat exchanger 230 exchanges heat with the first raw material to reduce the temperature, so as to prevent the coarse grinding machine 220 from being damaged due to overhigh temperature during continuous grinding. The first diaphragm pump 240 provides power for transporting the raw material. The raw material delivered from the blending subsystem 100 may be directly delivered to the rough grinding mill 220 for grinding, and then returned to the rough grinding tank 210, and the raw material is delivered from the rough grinding tank 210 to the rough grinding mill 220 for further grinding. Of course, the raw materials from the blending subsystem 100 may be directly transferred to the rough grinding tank 210 for storage, and then transferred from the rough grinding tank 210 to the rough grinding mill 220 for grinding, and the grinding cycle is returned to the rough grinding tank 210. When rough grinding is complete, it can be transported directly from the rough grinder 220 to the fine grinding subsystem 300, or from the rough grinding tank 210 to the fine grinding subsystem 300. How to set up specifically can design the pipeline according to actual demand.
Specifically, at least two sets of fine grinding subsystems 300 are provided, and the coarse grinding tank 210 and the coarse grinder 220 are connected to one end and then connected to each set of fine grinding subsystems 300. Each set of the fine grinding subsystems 300 includes at least two fine grinding tanks 310 connected in parallel and at least two fine grinders 320 connected in parallel. Each group of the fine grinding subsystems 300 operates independently, and the raw materials after the primary grinding treatment by the coarse grinding subsystem 200 are respectively conveyed to each group of the fine grinding subsystems 300. The fine grinding sub-system 300 can be two, three, four, or even more. The fine grinding subsystem 300 requires the raw material to be ground finer, so grinding is slower and longer. At least two sets of the fine grinding sub-systems 300 are provided to increase the grinding speed of the raw material.
As shown in fig. 4, the fine grinding subsystem 300 includes a second heat exchanger 330 and a second diaphragm pump 340; the second heat exchanger 330 and the second diaphragm pump 340 are disposed before the rough mill 220. The second heat exchanger 330 exchanges heat with the first raw material to reduce the temperature, so as to prevent the fine grinding machine 320 from being damaged due to overhigh temperature during continuous grinding. The second diaphragm pump 340 provides power for the delivery of the raw materials. The raw material delivered from the coarse grinding subsystem 200 may be directly delivered to the fine grinding machine 320 for grinding, and then returned to the fine grinding tank 310, and the raw material is delivered from the fine grinding tank 310 to the fine grinding machine 320 for further grinding. Of course, the raw material from the blending subsystem 100 may be directly transferred to the fine grinding tank 310 for storage, and then transferred from the fine grinding tank 310 to the fine grinding machine 320 for grinding, and the grinding cycle is returned to the fine grinding tank 310. When the fine grinding is completed, the slurry may be directly conveyed out of the fine grinding machine 320 or conveyed out of the fine grinding tank 310. How to set up specifically can design the pipeline according to actual demand.
As shown in fig. 5, the production system includes at least two sets of feeding subsystems 400, and each set of feeding subsystems 400 is connected to the mixing subsystem 100. Raw materials are transported through the feed subsystem 400 to the compounding subsystem 100. Specifically, the feeding subsystem 400 includes a feeding bin 410 and a metering bin 420, the feeding bin is connected to the metering bin 420, and the metering bin 420 is connected to the mixing subsystem 100. In a specific operation, the raw material is poured into the feeding bin 410, and the raw material in the feeding bin 410 is metered by the metering bin 420 and then conveyed to the mixing subsystem 100.
As shown in fig. 6, the production system includes at least two product tanks 500, and the finishing tank 310 and the finishing mill 320 are connected to the product tanks 500 after being connected to one end. The finishing tank 500 is used to store raw materials delivered from the fine grinding subsystem 300. A delivery pump 600 is disposed between the coarse grinding subsystem 200 and the fine grinding subsystem 300, and between the fine grinding subsystem 300 and the product tank 500. The transfer pump 600 provides power for transferring raw materials.
In the present invention, the rough grinding tank 210, the rough grinding machine 220, the fine grinding machine 320, the fine grinding tank 310, and other devices are connected through a pipeline 700, which is not described in detail herein.
The foregoing is a more detailed description of the utility model in connection with specific alternative embodiments, and the practice of the utility model should not be construed as limited to those descriptions. For those skilled in the art to which the utility model pertains, several simple deductions or substitutions can be made without departing from the spirit of the utility model, and all shall be considered as belonging to the protection scope of the utility model.
Claims (10)
1. A compounding grinds production system, its characterized in that includes:
the mixing subsystems are connected in parallel;
a coarse grinding subsystem comprising at least two coarse grinding tanks connected in parallel and at least two coarse mills connected in parallel; the rough grinding tank is connected to one end and then connected with the rough grinding machine; the mixing subsystem is connected to one end and then connected with the rough grinding subsystem;
the fine grinding subsystem comprises at least two fine grinding tanks connected in parallel and at least two fine grinders connected in parallel; the fine grinding tank is connected to one end and then connected with the fine grinding machine; the coarse grinding tank and the coarse grinding machine are connected to one end and then connected with the fine grinding subsystem.
2. The compounding mill production system of claim 1, wherein said fine grinding subsystems are provided in at least two sets, and said coarse grinding tank and said coarse grinder are connected to one end and then to each set of said fine grinding subsystems.
3. The compounding grinding production system of claim 1 or 2, wherein said production system includes at least two sets of feed subsystems, each set of said feed subsystems being connected to said compounding subsystem.
4. The compounding grinding production system of claim 1 or 2, wherein said production system comprises at least two product tanks, said finishing tank and said refiner being connected to one end and then to said product tanks, respectively.
5. The compounding mill production system of claim 1, wherein said compounding subsystem includes a compounding tank and a homogenizing pump; the batching tank and the homogenizing pump are connected and form a circulation loop.
6. The compounding grinding production system of claim 3, wherein the feed subsystem comprises a feed bin and a metering bin, the feed bin is connected to the metering bin, and the metering bin is connected to the compounding subsystem.
7. The compounding mill production system of claim 5, wherein said compounding subsystem includes a filter; the filter is arranged between the dosing tank and the homogenizing pump.
8. The compounding mill production system of claim 1, wherein said coarse grinding subsystem comprises a first heat exchanger and a first diaphragm pump; the first heat exchanger and the first diaphragm pump are arranged before the rough grinding machine.
9. The compounding mill production system of claim 1, wherein said fine grinding subsystem comprises a second heat exchanger and a second diaphragm pump; the second heat exchanger and the second diaphragm pump are arranged before the rough mill.
10. The compounding mill production system of claim 2, wherein a transfer pump is provided between the coarse grinding subsystem and the fine grinding subsystem, and between the fine grinding subsystem and the product tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121325223.7U CN215540452U (en) | 2021-06-15 | 2021-06-15 | Production system is ground to compounding |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121325223.7U CN215540452U (en) | 2021-06-15 | 2021-06-15 | Production system is ground to compounding |
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| Publication Number | Publication Date |
|---|---|
| CN215540452U true CN215540452U (en) | 2022-01-18 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202121325223.7U Active CN215540452U (en) | 2021-06-15 | 2021-06-15 | Production system is ground to compounding |
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| Country | Link |
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| CN (1) | CN215540452U (en) |
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2021
- 2021-06-15 CN CN202121325223.7U patent/CN215540452U/en active Active
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