CN218423376U - Concentrate production system - Google Patents
Concentrate production system Download PDFInfo
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- CN218423376U CN218423376U CN202222927802.XU CN202222927802U CN218423376U CN 218423376 U CN218423376 U CN 218423376U CN 202222927802 U CN202222927802 U CN 202222927802U CN 218423376 U CN218423376 U CN 218423376U
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Abstract
The utility model discloses a concentrate production system, including feeding machine, band conveyer, continuous ball grinder, ball grinding transfer barrel, sediment stuff pump, swirler, electromagnetism high frequency vibration sieve, sieve transfer barrel, deironing transfer barrel, electromagnetism magnetic separator, concentrate transfer barrel, cooling tower and tubing pump, electromagnetism magnetic separator includes first electromagnetism magnetic separator, second electromagnetism magnetic separator and third electromagnetism magnetic separator, the tubing pump includes first tubing pump; the water outlet of the cooling tower is communicated with the input end of the first pipeline pump, the output end of the first pipeline pump is respectively communicated with the water inlets of the first electromagnetic separator, the second electromagnetic separator and the third electromagnetic separator, and the water outlets of the first electromagnetic separator, the second electromagnetic separator and the third electromagnetic separator are all communicated with the water inlet of the cooling tower. The application has solved the water that has used through electromagnetic separator and has generally all directly discharged the external world, does not carry out cyclic utilization to it, causes the problem of the waste of water resource.
Description
Technical Field
The utility model relates to a concentrate production technical field specifically is a concentrate production system.
Background
In the process of concentrate production, raw ore is treated by a continuous ore mill to obtain ore pulp, and the ore pulp is subjected to filtration treatment such as iron removal to obtain concentrate. The filtering treatment for removing iron is generally carried out by adopting an electromagnetic separator, and when the electromagnetic separator works normally, a water source needs to be obtained from the outside to be supplied to the electromagnetic separator for use. The water used by the electromagnetic separator is generally directly discharged to the outside, and is not recycled, so that the waste of water resources is caused.
SUMMERY OF THE UTILITY MODEL
To the above-mentioned defect, the utility model provides a concentrate production system, aim at have solved and have used water through electromagnetic separator and generally all be the direct discharge external world, do not carry out cyclic utilization to it, cause the problem of the waste of water resource.
To achieve the purpose, the utility model adopts the following technical proposal:
a concentrate production system comprises a feeding machine, a belt conveyor, a continuous ball grinding machine, a ball grinding transfer barrel, a slurry pump, a cyclone, an electromagnetic high-frequency vibrating screen, a sieving transfer barrel, an iron removal transfer barrel, an electromagnetic separator, a concentrate transfer barrel, a cooling tower and a pipeline pump;
the belt conveyor comprises a first belt conveyor, the iron removal transfer barrel comprises a first iron removal transfer barrel, a second iron removal transfer barrel, a third iron removal transfer barrel and a fourth iron removal transfer barrel, the electromagnetic separator comprises a first electromagnetic separator, a second electromagnetic separator and a third electromagnetic separator, the pipeline pump comprises a first pipeline pump, and the slag slurry pump is provided with a plurality of pipeline pumps;
the output end of the feeding machine is communicated with the input end of the first belt conveyor, the output end of the first belt conveyor is communicated with the input end of the continuous ball grinder, the output end of the continuous ball grinder is communicated with the input end of the ball-milling transit barrel, the output end of the ball-milling transit barrel is communicated with the input end of the cyclone through the slurry pump, the surface row output end of the cyclone is communicated with the input end of the electromagnetic high-frequency vibrating screen, the output end of the electromagnetic high-frequency vibrating screen is communicated with the input end of the screening transit barrel, the output end of the screening transit barrel is communicated with the input end of the first iron-removing transit barrel through the slurry pump, the output end of the first iron-removing transit barrel is communicated with the input end of the first electromagnetic separator, the output end of the first electromagnetic separator is communicated with the input end of the second iron-removing transit barrel, the output end of the second iron-removing transit barrel is communicated with the input end of the third iron-removing transit barrel through the slurry pump, the output end of the third iron-removing transit barrel is communicated with the input end of the second electromagnetic separator, the output end of the second iron-removing transit barrel is communicated with the input end of the fourth electromagnetic separator, and the output end of the third iron-removing transit barrel is communicated with the input end of the electromagnetic separator;
the water outlet of the cooling tower is communicated with the input end of the first pipeline pump, the output end of the first pipeline pump is respectively communicated with the water inlets of the first electromagnetic separator, the second electromagnetic separator and the third electromagnetic separator, and the water outlets of the first electromagnetic separator, the second electromagnetic separator and the third electromagnetic separator are all communicated with the water inlet of the cooling tower.
Preferably, the system also comprises a concentrate concentrator, a concentrate bottom discharge barrel, a concentrate pressure filtration pulp storage pool, a pressure filtration feeding pump, a membrane pressure filter, a ton bag packing machine, a concentrate water pool and a concentrate bin, and the belt conveyor also comprises a second belt conveyor;
the output of the concentrate transit barrel passes through the sediment stuff pump communicate in the input of concentrate concentrator, the face of concentrate concentrator arrange the output communicate in the concentrate pond, the end of concentrate concentrator arrange the output communicate in the input of the end of concentrate row of bucket, the output of the end of concentrate row of bucket pass through the sediment stuff pump communicate in concentrate filter-pressing pulp storage pond, concentrate filter-pressing pulp storage pond still communicate in the input of pressure filter feeding pump, the output of pressure filter feeding pump communicate in the input of membrane pressure filter, the output of membrane pressure filter communicate respectively in the concentrate pond with the input of second belt conveyor, the output of second belt conveyor communicate in ton bag packagine machine's input, ton bag packagine machine's output communicate in the concentrate storehouse.
Preferably, the system further comprises a water storage tank, and the pipeline pump further comprises a second pipeline pump; the water storage tank is communicated with the input end of the second pipeline pump, and the output end of the second pipeline pump is communicated with the water replenishing port of the cooling tower.
Preferably, the concentrate pond is communicated with the filtrate input end of the continuous ball grinding machine through the slurry pump.
Preferably, the bottom row output end of the cyclone is communicated with the feed back input end of the continuous ball grinding machine.
Preferably, the output end of the second pipeline pump is also communicated with the concentrate water pool.
Preferably, the electromagnetic separator is a cylindrical electromagnetic separator.
The technical scheme provided by the embodiment of the application can have the following beneficial effects:
according to the scheme, the water outlet and the water inlet of the cooling tower are respectively communicated with the water inlets and the water outlets of the first electromagnetic separator, the second electromagnetic separator and the third electromagnetic separator, so that the cooling water can be recycled, and the waste of water resources is reduced.
Drawings
Fig. 1 is a schematic diagram of a concentrate production system;
FIG. 2 is an enlarged view of a portion of area A of FIG. 1;
fig. 3 is a partially enlarged view of the region B in fig. 1.
Wherein, 1, a feeder; 2. a belt conveyor; 3. a continuous ball grinding machine; 4. a grinding ball transferring barrel; 5. a slurry pump; 6. a swirler; 7. an electromagnetic high-frequency vibrating screen; 8. sieving and transferring to a barrel; 9. a deferrization transit barrel; 10. an electromagnetic separator; 11. a concentrate transferring barrel; 12. a concentrate concentrator; 13. a concentrate bottom discharge barrel; 14. a concentrate filter pressing pulp storage tank; 15. a filter press feeding pump; 16. a membrane filter press; 17. a ton bag packaging machine; 18. a concentrate pond; 19. a concentrate bin; 20. a cooling tower; 21. a pipeline pump; 22. a water storage tank; 91. a first iron removal transit barrel; 92. a second iron-removing transit barrel; 93. a third iron removing transit barrel; 94. a fourth iron removing transit barrel; 101. a first electromagnetic separator; 102. a second electromagnetic separator; 103. a third electromagnetic separator; 211. a first pipe pump; 212. a second pipe pump; 301. a filtrate input end; 302. a feed back input end; 601. a first surface row of output ends; 602. a first bottom row of output terminals; 1201. a second face row output end; 1202. a second bottom row of output terminals; 1011. a first water inlet; 1012. a first water outlet; 1021. a second water inlet; 1022. a second water outlet; 1031. a third water inlet; 1032. a third water outlet; 2001. and (4) water replenishing.
Detailed Description
The technical solution of the present invention is further explained by the following embodiments with reference to the accompanying drawings.
In the description of the present invention, it is to be understood that the terms "length", "middle", "upper", "lower", "left", "right", "top", "bottom", and the like, indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are used merely for convenience of description and simplification of description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, should not be construed as limiting the present invention.
Furthermore, the terms "first", "second" and "first" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature. In the description of the present invention, "a plurality" means two or more unless otherwise specified.
In the description of the present invention, it should be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "spliced" and "connected" are to be construed broadly, e.g., as being fixedly connected, detachably connected, or integrally connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
A concentrate production system comprises a feeding machine 1, a belt conveyor 2, a continuous ball grinding machine 3, a ball grinding transfer barrel 4, a slurry pump 5, a swirler 6, an electromagnetic high-frequency vibrating screen 7, a sieving transfer barrel 8, an iron removal transfer barrel 9, an electromagnetic separator 10, a concentrate transfer barrel 11, a cooling tower 20 and a pipeline pump 21;
the belt conveyor 2 comprises a first belt conveyor 201, the iron removing transit barrel 9 comprises a first iron removing transit barrel 91, a second iron removing transit barrel 92, a third iron removing transit barrel 93 and a fourth iron removing transit barrel 94, the electromagnetic separator 10 comprises a first electromagnetic separator 101, a second electromagnetic separator 102 and a third electromagnetic separator 103, the pipeline pump 21 comprises a first pipeline pump 211, and the slurry pump 5 is provided with a plurality of pumps;
the output end of the feeder 1 is communicated with the input end of the first belt conveyor 201, the output end of the first belt conveyor 201 is communicated with the input end of the continuous ball grinder 3, the output end of the continuous ball grinder 3 is communicated with the input end of the ball-grinding transfer drum 4, the output end of the ball-grinding transfer drum 4 is communicated with the input end of the cyclone 6 through the slurry pump 5, the surface row output end of the cyclone 6 is communicated with the input end of the electromagnetic high-frequency vibration sieve 7, the output end of the electromagnetic high-frequency vibration sieve 7 is communicated with the input end of the sieving transfer drum 8, the output end of the sieving transfer drum 8 is communicated with the input end of the first iron-removing transfer drum 91 through the slurry pump 5, the output end of the first iron-removing transfer drum 91 is communicated with the input end of the first electromagnetic magnetic separator 101, the output end of the first electromagnetic separator 101 is communicated with the input end of the second iron-removing transfer drum 92, the output end of the second iron-removing transfer drum 92 is communicated with the input end of the third iron-removing transfer drum 93 through the electromagnetic separator 5, the output end of the second iron-removing transfer drum 102 is communicated with the input end of the fourth electromagnetic separator 102, and the output end of the electromagnetic separator 93 is communicated with the input end of the second iron-removing electromagnetic separator 102;
a water outlet of the cooling tower 20 is communicated with an input end of the first pipeline pump 211, an output end of the first pipeline pump 211 is respectively communicated with water inlets of the first electromagnetic separator 101, the second electromagnetic separator 102 and the third electromagnetic separator 103, and water outlets of the first electromagnetic separator 101, the second electromagnetic separator 102 and the third electromagnetic separator 103 are all communicated with a water inlet of the cooling tower 20.
For better understanding of the solution of the present embodiment, as shown in fig. 1 to 3, the surface row output end of the cyclone 6 is referred to as a first surface row output end 601; the bottom row output end of the cyclone 6 is called a first bottom row output end 602; the surface row output end of the concentrate concentrator 12 is called a second surface row output end 1201; the bottom row of outputs of the concentrate concentrator 12 is referred to as the second bottom row of outputs 1202.
The water inlet of the first electromagnetic separator 101 is called as a first water inlet 1011; the water inlet of the second electromagnetic separator 102 is called as a second water inlet 1021; the water inlet of the third electromagnetic separator 103 is called third water inlet 1031; a water outlet of the first electromagnetic separator 101 is called as a first water outlet 1012; the water outlet of the second electromagnetic separator 102 is called as a second water outlet 1022; the water outlet of the third electromagnetic separator 103 is called a third water outlet 1032.
In order to better distinguish the ore pulp and the concentrate water obtained in each treatment step, the ore pulp is divided into a first ore pulp, a second ore pulp, a third ore pulp, a fourth ore pulp, a fifth ore pulp, a sixth ore pulp, a seventh ore pulp, an eighth ore pulp and a ninth ore pulp, and the concentrate water is divided into a first concentrate water and a second concentrate water.
The utility model provides a concentrate filters production system puts into the raw ore feeder 1, feeder 1 can carry out preliminary screening to the raw ore, clears away some major impurities in the raw ore and filters, obtains useful raw ore, and useful raw ore passes through feeder 1 is supplied continuously, evenly and is carried first band conveyer 201, the rethread first band conveyer 201 carries continuous ball grinder 3, continuous ball grinder 3 can be in succession, effectively smash useful raw ore into the ore grain, forms first ore pulp behind the ore grain pulp. First ore pulp gets into ball transfer bucket 4 temporarily stores, the rethread slurry pump 5, slurry pump 5 can clear away the solid-like slurry of ore pulp granule and obtain the second ore pulp. The second ore pulp enters the cyclone 6, and the cyclone 6 is used for grading, sorting, concentrating and desliming the second ore pulp, so that the heavier solid particles in the second ore pulp sink to the bottom and the lighter solid particles float to the surface. The second ore pulp containing lighter solid particles is discharged into the electromagnetic high-frequency vibrating screen 7, and the electromagnetic high-frequency vibrating screen 7 adopts high frequency, so that the second ore pulp can be effectively separated from solid and crushed ore, and third ore pulp is obtained. And the third ore pulp enters the sieving transfer barrel 8 for temporary storage, and then the fourth ore pulp is obtained through the slurry pump 5. The fourth ore pulp enters the first iron removal transfer barrel 91 for temporary storage, and then is subjected to iron removal treatment by the first electromagnetic separator 101 to obtain fifth ore pulp. The fifth pulp passes through the second iron removal transfer drum 92 for temporary storage, and passes through the third slurry pump 53, to obtain a sixth pulp. And the sixth ore pulp enters the third iron removal transfer barrel 93 for temporary storage, and then is sent to the second electromagnetic separator 102 for iron removal treatment, so that seventh ore pulp is obtained. The seventh ore pulp enters the fourth iron removal transfer barrel 94 for temporary storage, and then is subjected to iron removal treatment by the third electromagnetic separator 103, so that eighth ore pulp is obtained. And the eighth ore pulp is sequentially treated to obtain ninth ore pulp, first concentrate water and second concentrate water, and finally concentrate is obtained.
The cooling water in the cooling tower 20 is pumped to the first electromagnetic separator 101, the second electromagnetic separator 102 and the third electromagnetic separator 103 through the first pipeline pump 211 for cooling, and the first electromagnetic separator 101, the second electromagnetic separator 102 and the third electromagnetic separator 103 can transport the used cooling water back to the cooling tower 20 again, so that the recycling of the cooling water is realized.
In the scheme, the water outlet and the water inlet of the cooling tower 20 are respectively communicated with the water inlets and the water outlets of the first electromagnetic separator 101, the second electromagnetic separator 102 and the third electromagnetic separator 103, so that the cyclic utilization of cooling water is facilitated, and the waste of water resources is reduced.
Preferably, the system also comprises a concentrate concentrator 12, a concentrate bottom discharge barrel 13, a concentrate press filtration pulp storage tank 14, a press filter feeding pump 15, a membrane press filter 16, a ton bag packing machine 17, a concentrate water tank 18 and a concentrate bin 19, and the belt conveyor 2 also comprises a second belt conveyor 202;
the output of the concentrate transit barrel 11 passes through the slurry pump 5 communicate in the input of the concentrate concentrator 12, the face of the concentrate concentrator 12 is arranged the output and is communicated in the concentrate pond 18, the end of the concentrate concentrator 12 is arranged the output and is communicated in the input of the concentrate end is arranged the barrel 13, the output of the concentrate end is arranged the barrel 13 and is passed through the slurry pump 5 communicate in the concentrate filter-pressing pulp storage pond 14, the concentrate filter-pressing pulp storage pond 14 still communicate in the input of the filter-pressing feeding pump 15, the output of the filter-pressing feeding pump 15 communicate in the input of the membrane filter press 16, the output of the membrane filter press 16 communicate respectively in the concentrate pond 18 with the input of the second belt conveyor 202, the output of the second belt conveyor 202 communicate in the input of the ton bag packing machine 17, the output of the ton bag packing machine 17 communicate in the concentrate storehouse 19.
In this embodiment, as shown in fig. 1, the eighth slurry enters the concentrate transferring barrel 11 for temporary storage, and then passes through the slurry pump 5 to obtain a ninth slurry. The ninth ore pulp gets into concentrate concentrator 12, concentrate concentrator 12 can concentrate and filter the ore pulp, obtains first concentrate water and concentrate filtrating, and wherein, concentrate filtrating can directly arrange into concentrate pond 18 carries out cyclic utilization, and first concentrate water gets into arrange bucket 13 at the bottom of the concentrate temporarily stores, and first concentrate water passes through sediment stuff pump 5 obtains the second concentrate water. The second concentrate water enters the concentrate filter-pressing pulp storage tank 14 for temporary storage, and is pumped into the membrane filter press 16 through the filter press feeding pump 15, the membrane filter press 16 can effectively perform filter-pressing treatment on the second concentrate water to obtain concentrate and concentrate filtrate, and the concentrate is conveyed to the ton bag packing machine 17 through the second belt conveyor 202, so that the concentrate can be conveniently bagged and packed, and finally conveyed to the concentrate bin 19 for storage, and the production of the concentrate is realized; concentrate filtrate is discharged into the concentrate water tank 18 for recycling.
Preferably, the system further comprises a water storage tank 22, and the pipeline pump 21 further comprises a second pipeline pump 212; the water storage tank 22 is communicated with the input end of the second pipeline pump 212, and the output end of the second pipeline pump 212 is communicated with the water replenishing port 2001 of the cooling tower 20.
In this embodiment, as shown in fig. 1, the water in the water storage 22 may be pumped to the cooling tower 20 by the second pipeline pump 21, so as to realize automatic water replenishment of the cooling tower 20, and ensure that the cooling tower 20 is continuously replenished with water and cooled. To further illustrate, the water in the reservoir 22 may also be used for both shop life water and test water.
Preferably, the concentrate pond 18 is communicated with a filtrate input end 301 of the continuous ball grinding machine 3 through the slurry pump 5. In this embodiment, as shown in fig. 2, the concentrate filtrate in the concentrate pond 18 can be supplied to the continuous ball grinding machine 3 through the slurry pump 5, which is beneficial to recycling the concentrate filtrate.
Preferably, the bottom row output end of the cyclone 6 is communicated with the feed back input end 302 of the continuous ball grinding machine 3. In this embodiment, as shown in fig. 2, the second slurry containing the heavier solid particles is discharged back to the continuous ball mill 3, and the continuous ball mill 3 grinds the second slurry again, so as to effectively reduce the heavier solid particles in the slurry.
Preferably, the output end of the second pipe pump 212 is also communicated with the concentrate pond 18. In this embodiment, as shown in fig. 1, the water in the storage tank 22 can be pumped into the concentrate tank 18 through the second pipe pump 212, which is beneficial to replenishing the concentrate tank 18.
Preferably, the electromagnetic separator 10 is a cylindrical electromagnetic separator. In this embodiment, the electromagnetic separator 10 is a cylindrical electromagnetic separator, which has a simple structure, high material separation accuracy, and high work efficiency.
The technical principle of the present invention is described above with reference to specific embodiments. The description is made for the purpose of illustrating the principles of the invention and should not be construed in any way as limiting the scope of the invention. Based on the explanations herein, those skilled in the art will be able to conceive of other embodiments of the present invention without any inventive effort, which would fall within the scope of the present invention.
Claims (7)
1. A concentrate production system, its characterized in that: the device comprises a feeding machine, a belt conveyor, a continuous ball grinding machine, a ball grinding transfer barrel, a slurry pump, a swirler, an electromagnetic high-frequency vibrating screen, a sieving transfer barrel, an iron removal transfer barrel, an electromagnetic magnetic separator, a concentrate transfer barrel, a cooling tower and a pipeline pump;
the belt conveyor comprises a first belt conveyor, the iron removal transfer barrel comprises a first iron removal transfer barrel, a second iron removal transfer barrel, a third iron removal transfer barrel and a fourth iron removal transfer barrel, the electromagnetic separator comprises a first electromagnetic separator, a second electromagnetic separator and a third electromagnetic separator, the pipeline pump comprises a first pipeline pump, and the slag slurry pump is provided with a plurality of pipeline pumps;
the output end of the feeding machine is communicated with the input end of the first belt conveyor, the output end of the first belt conveyor is communicated with the input end of the continuous ball grinder, the output end of the continuous ball grinder is communicated with the input end of the ball-milling transit barrel, the output end of the ball-milling transit barrel is communicated with the input end of the cyclone through the slurry pump, the surface row output end of the cyclone is communicated with the input end of the electromagnetic high-frequency vibrating screen, the output end of the electromagnetic high-frequency vibrating screen is communicated with the input end of the screening transit barrel, the output end of the screening transit barrel is communicated with the input end of the first iron-removing transit barrel through the slurry pump, the output end of the first iron-removing transit barrel is communicated with the input end of the first electromagnetic separator, the output end of the first electromagnetic separator is communicated with the input end of the second iron-removing transit barrel, the output end of the second iron-removing transit barrel is communicated with the input end of the third iron-removing transit barrel through the slurry pump, the output end of the third iron-removing transit barrel is communicated with the input end of the second electromagnetic separator, the output end of the second iron-removing transit barrel is communicated with the input end of the fourth electromagnetic separator, and the output end of the third iron-removing transit barrel is communicated with the input end of the electromagnetic separator;
the water outlet of the cooling tower is communicated with the input end of the first pipeline pump, the output end of the first pipeline pump is respectively communicated with the water inlets of the first electromagnetic separator, the second electromagnetic separator and the third electromagnetic separator, and the water outlets of the first electromagnetic separator, the second electromagnetic separator and the third electromagnetic separator are all communicated with the water inlet of the cooling tower.
2. A concentrate production system according to claim 1, characterized in that: the device comprises a concentrate concentrator, a concentrate bottom discharge barrel, a concentrate filter-pressing pulp storage pool, a filter press feeding pump, a membrane filter press, a ton bag packing machine, a concentrate pool and a concentrate bin, wherein the belt conveyor further comprises a second belt conveyor;
the output of the concentrate transit barrel passes through the sediment stuff pump communicate in the input of concentrate concentrator, the face of concentrate concentrator arrange the output communicate in the concentrate pond, the end of concentrate concentrator arrange the output communicate in the input of the end of concentrate row of bucket, the output of the end of concentrate row of bucket pass through the sediment stuff pump communicate in concentrate filter-pressing pulp storage pond, concentrate filter-pressing pulp storage pond still communicate in the input of pressure filter feeding pump, the output of pressure filter feeding pump communicate in the input of membrane pressure filter, the output of membrane pressure filter communicate respectively in the concentrate pond with the input of second belt conveyor, the output of second belt conveyor communicate in ton bag packagine machine's input, ton bag packagine machine's output communicate in the concentrate storehouse.
3. A concentrate production system according to claim 2, characterized in that: the pipeline pump also comprises a water storage tank and a second pipeline pump; the water storage tank is communicated with the input end of the second pipeline pump, and the output end of the second pipeline pump is communicated with the water replenishing port of the cooling tower.
4. A concentrate production system according to claim 2, characterized in that: the concentrate pond passes through the sediment stuff pump communicate in continuous ball grinder's filtrating input.
5. A concentrate production system according to claim 1, characterized in that: and the bottom row output end of the cyclone is communicated with the feed back input end of the continuous ball grinding machine.
6. A concentrate production system according to claim 3, characterized in that: and the output end of the second pipeline pump is also communicated with the concentrate water tank.
7. A concentrate production system according to claim 1, characterized in that: the electromagnetic separator is a cylindrical electromagnetic separator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222927802.XU CN218423376U (en) | 2022-11-01 | 2022-11-01 | Concentrate production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222927802.XU CN218423376U (en) | 2022-11-01 | 2022-11-01 | Concentrate production system |
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| Publication Number | Publication Date |
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| CN218423376U true CN218423376U (en) | 2023-02-03 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202222927802.XU Active CN218423376U (en) | 2022-11-01 | 2022-11-01 | Concentrate production system |
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| CN (1) | CN218423376U (en) |
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