CN213915433U - Electrolytic manganese slag treatment system - Google Patents
Electrolytic manganese slag treatment system Download PDFInfo
- Publication number
- CN213915433U CN213915433U CN202022541918.0U CN202022541918U CN213915433U CN 213915433 U CN213915433 U CN 213915433U CN 202022541918 U CN202022541918 U CN 202022541918U CN 213915433 U CN213915433 U CN 213915433U
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- China
- Prior art keywords
- storehouse
- stirring
- electrolytic manganese
- manganese slag
- fixed mounting
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- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 title claims abstract description 46
- 229910052748 manganese Inorganic materials 0.000 title claims abstract description 45
- 239000011572 manganese Substances 0.000 title claims abstract description 45
- 239000002893 slag Substances 0.000 title claims description 35
- 238000003756 stirring Methods 0.000 claims abstract description 51
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000000463 material Substances 0.000 claims abstract description 13
- 238000012545 processing Methods 0.000 claims abstract description 13
- 230000008878 coupling Effects 0.000 claims abstract description 7
- 238000010168 coupling process Methods 0.000 claims abstract description 7
- 238000005859 coupling reaction Methods 0.000 claims abstract description 7
- 239000013049 sediment Substances 0.000 claims abstract description 5
- 238000009833 condensation Methods 0.000 claims description 20
- 230000005494 condensation Effects 0.000 claims description 20
- 238000007599 discharging Methods 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 239000002994 raw material Substances 0.000 abstract description 11
- 229910021529 ammonia Inorganic materials 0.000 abstract description 7
- 238000013329 compounding Methods 0.000 abstract description 6
- 230000006872 improvement Effects 0.000 abstract description 4
- 238000005520 cutting process Methods 0.000 abstract description 3
- 238000013461 design Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 10
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 230000000149 penetrating effect Effects 0.000 description 6
- 230000007547 defect Effects 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 229910001385 heavy metal Inorganic materials 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910000914 Mn alloy Inorganic materials 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- ZCCIPPOKBCJFDN-UHFFFAOYSA-N calcium nitrate Chemical compound [Ca+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ZCCIPPOKBCJFDN-UHFFFAOYSA-N 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000011464 hollow brick Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Inorganic materials [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 1
- 235000010333 potassium nitrate Nutrition 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000035899 viability Effects 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
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- Processing Of Solid Wastes (AREA)
Abstract
The utility model belongs to the technical field of the electrolytic manganese sediment, especially, be an electrolytic manganese sediment processing system, including the stirring storehouse, first motor is installed to stirring storehouse top bolt, first motor output passes through coupling joint and installs first axis of rotation, first axis of rotation bottom runs through and extends to in the stirring storehouse and the joint installs the stirring leaf, the discharge is installed in pegging graft on one side of stirring storehouse top, the ammonia collecting box is installed in the grafting on the discharge top, the pan feeding pipe is installed in the grafting of stirring storehouse top, the row's of installing material pipe is pegged graft on one side of stirring storehouse bottom, it has crushing storehouse to arrange material pipe bottom grafting connection, it has the lifter to smash storehouse inner wall bottom welded mounting, lifter top welded mounting has lifting bottom plate. The utility model discloses true problem reasonable in design, easy operation, convenient to use, the compounding is even and the operation continuity is complete, to the effectual processing of cutting apart of the raw materials in mixed later stage, further improvement the treatment effeciency.
Description
Technical Field
The utility model relates to an electrolytic manganese sediment technical field especially relates to an electrolytic manganese sediment processing system.
Background
With the rapid development of steel and nonferrous metal industry in China, manganese and manganese alloy are indispensable raw materials as additives, deoxidizers and desulfurizers in the steel and nonferrous metal industry, the demand of the manganese and manganese alloy is continuously increased, and the electrolytic manganese metal industry is also pulled to rapidly develop.
Along with the increasing of the manganese yield, the problems brought by electrolytic manganese slag are serious, a large amount of piled manganese slag generates huge pressure on the environment and causes waste of resources, so a process route for resource utilization of manganese slag is required to be found, the electrolytic manganese slag is filter-pressing residue generated after manganese is prepared by an electrolytic method in the electrolytic manganese industry, the electrolytic manganese slag after filter-pressing is acidic and blocky (25-27% of water), the average particle size is only 44 mu m with large specific gravity (2.64g/cm3), the viscosity is large under natural conditions, and the electrolytic manganese slag contains various heavy metals, ammonia nitrogen and other environmental pollutants. Meanwhile, the electrolytic manganese slag has higher water content and large volume, and brings difficulty to stacking and transportation.
At present, a mature treatment technology aiming at electrolytic manganese slag is available, but core stirring equipment for realizing the technology is lacked, the industry of the electrolytic manganese slag treatment technology is restricted, gas generated by high-temperature treatment of organic matters such as ammonia, nitrogen, sulfur, carbon and the like removed from the electrolytic manganese slag is directly exhausted only through desorption treatment, secondary pollution is generated, and the essential requirements of China on harmless treatment of industrial solid pollution are not met.
However, the utilization of manganese slag in China is still in a primary stage, the technology is yet to be mature, and the existing treatment method has serious defects: firstly, the electrolytic manganese slag fine micro powder clinker without organic matters such as ammonia, nitrogen, sulfur, carbon and the like is sold to a cement plant as a retarder at the price of about 100 yuan/ton in the prior method, and because the retarder is prepared, a large amount of fire coal is consumed, and the modified materials such as blended lime, soda and the like are high in cost, the phenomenon that an enterprise is not laid out is finally caused, and the independent viability is lacked; secondly, gas generated by high-temperature removal of organic matters such as ammonia, nitrogen, sulfur, carbon and the like from the electrolytic manganese slag is directly exhausted only through desorption treatment, secondary pollution is generated, and the essential requirements of the state on harmless treatment of industrial solid pollution are not met; in addition, heavy metal elements such as manganese, iron, chromium, cadmium and the like contained in the electrolytic manganese slag still remain in the roasted fine powder material in the form of oxides, if the material containing heavy metals is used for directly firing building materials such as hollow bricks and the like, the problems of saltpeter return, blocking removal, weathering and the like are easy to occur, so that the subsequent resource utilization of the material is seriously influenced, the key of the electrolytic manganese slag treatment is the dispersion of the manganese slag and the sufficient mixing and reaction of a treating agent and the manganese slag, but the problems and the defects of difficult feeding and discharging, discontinuous operation, uneven mixing, low dispersion degree, insufficient control of ammonia gas, easy burning of a stirrer motor and the like are easily generated in the electrolytic manganese slag treatment process, and some unit researches adopt the modes of drying, airing and the like to pre-dry the electrolytic manganese slag, effectively crush the electrolytic manganese slag after the water content is reduced to 10%, and then treat the electrolytic manganese slag. However, the method has the defects of long period, high cost, large occupied area and the like, and is not the best solution, and the existing manganese slag utilization technology has the defects of high cost, environmental pollution and substandard product quality, so that the electrolytic manganese slag treatment system is provided.
SUMMERY OF THE UTILITY MODEL
The utility model aims at solving the defects existing in the prior art and providing an electrolytic manganese slag treatment system.
In order to achieve the above purpose, the utility model adopts the following technical scheme: an electrolytic manganese slag treatment system comprises a stirring bin, wherein a first motor is installed on the top end of the stirring bin through a bolt, a first rotating shaft is installed at the output end of the first motor through a coupling joint, the bottom end of the first rotating shaft extends into the stirring bin in a penetrating manner and is connected with stirring blades in a clamping manner, a gas collecting pipe is installed on one side of the top end of the stirring bin in a penetrating manner, an ammonia collecting box is installed on the top end of the gas collecting pipe in a penetrating manner, a feeding pipe is installed on the top end of the stirring bin in a penetrating manner, a discharging pipe is installed on one side of the bottom end of the stirring bin in a penetrating manner, a crushing bin is connected with the bottom end of the discharging pipe in a penetrating manner, a lifting rod is installed on the bottom end of the inner wall of the crushing bin in a welding manner, a lifting bottom plate is installed on the top end of the lifting rod in a welding manner, a second motor is installed on the bottom end of the crushing bin through a coupling joint, a second rotating shaft penetrates through the lifting bottom plate and is installed with crushing blades through the bolt, smash storehouse one side and be connected with the condensation storehouse through pipeline grafting, condensation storehouse inner wall top welded mounting has the connecting rod, connecting rod bottom welded mounting has the condensation tank, condensation storehouse one side is connected with refrigerating plant through pipeline grafting, stirring storehouse one side joint is installed the controller.
Preferably, the gas collecting pipe, the feeding pipe and the discharging pipe are all connected with and provided with electromagnetic valves.
Preferably, the bottom end of the condensation bin is connected with a water guide pipe in an inserting manner.
Preferably, the two sides of the bottom end of the stirring bin are welded with brackets.
Preferably, the feeding pipes are two and are arranged side by side, one is a water inlet pipe, and the other is a feeding pipe.
Preferably, the stirring bin is in an inverted trapezoid shape, and the stirring blades are arranged in a height-width mode.
Preferably, an external power supply and a switch are arranged on one side of the support, wherein the external power supply, the first motor, the second motor, the crushing blade, the refrigerating device and the switch are sequentially connected through a lead and form a loop.
Preferably, the controller, the electromagnetic valve, the crushing blade and the refrigerating device are electrically connected.
Compared with the prior art, the beneficial effects of the utility model are that: during the use pan feeding pipe is put in the raw materials to stirring the storehouse in, start first motor, drive the stirring leaf through first axis of rotation and stir the raw materials, wherein the ammonia that produces passes through the discharge tube and collects to the ammonia collecting box in, the raw materials of mixing flows to smashing in the storehouse through the discharge pipe, it dries and heats to smash the compounding in the storehouse to smash the blade winding simultaneously, the second motor drives through the second axis of rotation and smashes the blade and smashes the compounding, the steam of while production passes through the pipeline and discharges to the condensation storehouse in, refrigerating plant does work and cools down the condensate tank in the condensation storehouse, steam meets the cold condensation and condenses on the condensate tank surface, discharge from the aqueduct at last, kibbling compounding can discharge through reducing the discharging pipe that makes the lifting bottom plate through smashing storehouse one side with the lifter.
The utility model discloses true problem reasonable in design, easy operation, convenient to use, the compounding is even and the operation continuity is complete, to the effectual processing of cutting apart of the raw materials in mixed later stage, advances one improvement the treatment effeciency.
Drawings
FIG. 1 is a front sectional view of the present invention;
fig. 2 is a schematic front view of the external structure of the present invention;
fig. 3 is a schematic top view of the external structure of the present invention;
fig. 4 is a schematic perspective view of a condensation tank according to the present invention;
in the figure: 1. a stirring bin; 2. a first motor; 3. a first rotating shaft; 4. stirring blades; 5. a gas collecting pipe; 6. an ammonia gas collecting box; 7. a feeding pipe; 8. a discharge pipe; 9. a crushing bin; 10. a lifting rod; 11. a lifting bottom plate; 12. a second motor; 13. a second rotating shaft; 14. crushing the leaves; 15. a condensation bin; 16. a connecting rod; 17. a condensation tank; 18. A refrigeration device; 19. a controller; 20. an electromagnetic valve; 21. a water conduit; 22. and (4) a bracket.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-4, the present invention provides a technical solution: an electrolytic manganese slag treatment system comprises a stirring bin 1, wherein a first motor 2 is fixedly installed at the top end of the stirring bin 1, a first rotating shaft 3 is installed at the output end of the first motor 2 through a coupling joint, the bottom end of the first rotating shaft 3 penetrates into the stirring bin 1 and is fixedly provided with a stirring blade 4, a gas collecting pipe 5 is fixedly installed at one side of the top end of the stirring bin 1, an ammonia gas collecting box 6 is fixedly installed at the top end of the gas collecting pipe 5, a feeding pipe 7 is fixedly installed at the top end of the stirring bin 1, a discharging pipe 8 is fixedly installed at one side of the bottom end of the stirring bin 1, a crushing bin 9 is fixedly connected with the bottom end of the discharging pipe 8, a lifting rod 10 is fixedly installed at the bottom end of the inner wall of the crushing bin 9, a lifting bottom plate 11 is fixedly installed at the top end of the lifting rod 10, a second motor 12 is fixedly installed at the bottom end of the crushing bin 9, a second rotating shaft 13 is installed at the top end of the second rotating shaft 13 through the coupling joint and is fixedly installed with a crushing blade 14, a condensation bin 15 is fixedly connected to one side of the crushing bin 9 through a pipeline, a connecting rod 16 is fixedly installed at the top end of the inner wall of the condensation bin 15, a condensation tank 17 is fixedly installed at the bottom end of the connecting rod 16, a refrigerating device 18 is fixedly connected to one side of the condensation bin 15 through a pipeline, and a controller 19 is fixedly installed at one side of the stirring bin 1;
the gas collecting pipe 5, the feeding pipe 7 and the discharging pipe 8 are respectively connected with and provided with an electromagnetic valve 20, so that the flow of raw materials is conveniently controlled, and the convenience in improvement is further realized; the bottom end of the condensation bin 15 is fixedly connected with a water guide pipe 21, so that the water guide pipe can be effectively recycled, and the environment pollution caused by waste gas can be prevented; the two sides of the bottom end of the stirring bin 1 are fixedly provided with the supports 22, so that the stability of the whole device is provided; the two feeding pipes 7 are arranged side by side, one is a water inlet pipe, and the other is a feeding pipe, so that feeding is conveniently connected; the stirring bin 1 is in an inverted trapezoid shape, the stirring blades 4 are arranged in a high-width-low-width mode, and when the stirring bin is placed, mixed and stirred, viscous force causes damage to a motor, so that stirring and discharging are facilitated; an external power supply and a switch are arranged on one side of the bracket 22, wherein the external power supply, the first motor 2, the second motor 12, the crushing blade 14, the refrigerating device 18 and the switch are sequentially connected through a lead to form a loop; the controller 19, the electromagnetic valve 20, the crushing blade 14 and the refrigerating device 18 are electrically connected, and operation is convenient.
The working principle is as follows: when in use, the material feeding pipe 7 feeds raw materials into the stirring bin 1, the first motor 2 is started, the stirring blade 4 is driven by the first rotating shaft 3 to stir the raw materials, the generated ammonia gas is collected into the ammonia gas collecting box 6 through the gas collecting pipe 5, the mixed raw materials flow into the crushing bin 9 through the material discharging pipe 8, the crushing blade 14 is wound to dry and heat the mixed material in the crushing bin 9, the second motor 12 drives the crushing blade 14 to crush the mixed material through the second rotating shaft 13, the generated hot gas is discharged into the condensing bin 15 through a pipeline, the refrigerating device 18 is used for cooling the condensing tank 17 in the condensing bin 15, the hot gas is condensed on the surface of the condensing tank 17 when encountering cold and is discharged from the water guide pipe 21, and the crushed mixed material can be discharged through the discharging pipe on one side of the crushing bin 9 by lowering the lifting bottom plate 11 through the lifting rod 10, the utility model has reasonable design, easy operation, convenient to use, the compounding is even and the operation continuity is complete, to the effectual processing of cutting apart of the raw materials in mixed later stage, one improvement the treatment effeciency.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (8)
1. The utility model provides an electrolytic manganese sediment processing system, includes stirring storehouse (1), its characterized in that: a first motor (2) is fixedly installed at the top end of the stirring bin (1), a first rotating shaft (3) is installed at the output end of the first motor (2) through a coupling, the bottom end of the first rotating shaft (3) penetrates through the stirring bin (1) and is fixedly provided with stirring blades (4), a gas collecting pipe (5) is fixedly installed on one side of the top end of the stirring bin (1), and an ammonia gas collecting box (6) is fixedly installed at the top end of the gas collecting pipe (5); stirring storehouse (1) top fixed mounting has pan feeding pipe (7), stirring storehouse (1) bottom one side fixed mounting has row material pipe (8), it smashes storehouse (9) to arrange material pipe (8) bottom fixedly connected with, it has lifter (10) to smash storehouse (9) inner wall bottom fixed mounting, lifter (10) top fixed mounting has elevator (11), it has second motor (12) to smash storehouse (9) bottom fixed mounting, second motor (12) output is installed through the coupling joint second axis of rotation (13), second axis of rotation (13) top runs through elevator (11) and fixed mounting has crushing blade (14), it has condensation storehouse (15) through pipeline fixedly connected with to smash storehouse (9) one side, condensation storehouse (15) inner wall top fixed mounting has connecting rod (16), connecting rod (16) bottom fixed mounting has condensation tank (17), condensing bin (15) one side is through pipeline fixedly connected with refrigerating plant (18), stirring bin (1) one side fixed mounting has controller (19).
2. The electrolytic manganese slag processing system according to claim 1, wherein: and the gas collecting pipe (5), the feeding pipe (7) and the discharging pipe (8) are all connected with and provided with electromagnetic valves (20).
3. The electrolytic manganese slag processing system according to claim 1, wherein: the bottom end of the condensation bin (15) is fixedly connected with a water guide pipe (21).
4. The electrolytic manganese slag processing system according to claim 1, wherein: and supports (22) are fixedly arranged on two sides of the bottom end of the stirring bin (1).
5. The electrolytic manganese slag processing system according to claim 1, wherein: pan feeding pipe (7) have two, and install together side by side, one is the inlet tube, and another is the inlet tube.
6. The electrolytic manganese slag processing system according to claim 1, wherein: the stirring bin (1) is in an inverted trapezoid shape, and the stirring blades (4) are arranged in a high-width and low-width mode.
7. The electrolytic manganese slag processing system according to claim 4, wherein: an external power supply and a switch are arranged on one side of the support (22), wherein the external power supply, the first motor (2), the second motor (12), the crushing blade (14), the refrigerating device (18) and the switch are sequentially connected through a lead and form a loop.
8. The electrolytic manganese slag processing system according to claim 1, wherein: the controller (19), the electromagnetic valve (20), the crushing blade (14) and the refrigerating device (18) are electrically connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022541918.0U CN213915433U (en) | 2020-11-06 | 2020-11-06 | Electrolytic manganese slag treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022541918.0U CN213915433U (en) | 2020-11-06 | 2020-11-06 | Electrolytic manganese slag treatment system |
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| Publication Number | Publication Date |
|---|---|
| CN213915433U true CN213915433U (en) | 2021-08-10 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022541918.0U Expired - Fee Related CN213915433U (en) | 2020-11-06 | 2020-11-06 | Electrolytic manganese slag treatment system |
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| Country | Link |
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| CN (1) | CN213915433U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115382886A (en) * | 2022-08-10 | 2022-11-25 | 桂林理工大学 | Mechanical homogenization-low-temperature thermal activation accurate harmless treatment method for electrolytic manganese slag |
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2020
- 2020-11-06 CN CN202022541918.0U patent/CN213915433U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115382886A (en) * | 2022-08-10 | 2022-11-25 | 桂林理工大学 | Mechanical homogenization-low-temperature thermal activation accurate harmless treatment method for electrolytic manganese slag |
| CN115382886B (en) * | 2022-08-10 | 2023-06-20 | 桂林理工大学 | Mechanical homogenization-low-temperature thermal activation accurate harmless treatment method for electrolytic manganese slag |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20210810 |
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| CF01 | Termination of patent right due to non-payment of annual fee |