CN218610615U - Silver electrolysis residual anode washing tank - Google Patents
Silver electrolysis residual anode washing tank Download PDFInfo
- Publication number
- CN218610615U CN218610615U CN202220963286.3U CN202220963286U CN218610615U CN 218610615 U CN218610615 U CN 218610615U CN 202220963286 U CN202220963286 U CN 202220963286U CN 218610615 U CN218610615 U CN 218610615U
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- CN
- China
- Prior art keywords
- cell body
- utility
- model
- anode
- wash
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- 238000005406 washing Methods 0.000 title claims abstract description 23
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 16
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 title claims abstract description 14
- 229910052709 silver Inorganic materials 0.000 title claims abstract description 14
- 239000004332 silver Substances 0.000 title claims abstract description 14
- 210000005056 cell body Anatomy 0.000 claims abstract description 12
- 238000001914 filtration Methods 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 7
- 238000002791 soaking Methods 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000004744 fabric Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 206010050031 Muscle strain Diseases 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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- Electrolytic Production Of Metals (AREA)
Abstract
The utility model provides a silver electrolysis anode scrap sink, includes the cell body, be equipped with the filtration baffle in the cell body, be equipped with 2 runner tracks on it, the cell body both sides are equipped with bow-shaped splashproof baffle, bow-shaped splashproof baffle is equipped with two buckles, the cell body bottom is equipped with the feed liquid outlet. The utility model discloses not only have and wash extremely convenient, light, swift characteristics of incomplete, still have the function of dashing the bubble positive pole mud simultaneously, can alleviate post personnel's intensity of labour by a wide margin, its rational in infrastructure, easy operation is convenient, strong adaptability, even if women's will also operate, do not choose the people. The utility model is used for wash the anode scrap, collect and wash the water and be used for soaking and washing the anode slime, this link of liquid is reduced in whole operation, but the while using water wisely shortens production cycle, raises the efficiency.
Description
Technical Field
The utility model relates to the technical field of metallurgical equipment, in particular to a silver electrolysis residual anode washing tank.
Background
Along with the intensive work of enterprises, the production of silver is increased, and simultaneously, a large amount of anode scrap is generated in silver electrolysis, so that the anode scrap rate needs to be reduced for improving the silver yield and reducing furnace return, the electrolysis anode scrap needs to be washed for secondary electrolysis, and the washing effect influences the secondary electrolysis effect.
At present, an electrolysis factory washes anode scraps completely by manual operation, each anode scrap weighs about 10kg, in the washing process, overturning is completely by manual operation, washing is also performed by a brush, the labor intensity is high, the lumbar muscle strain is serious, and the efficiency is low, so that the method is not suitable for large-scale production.
SUMMERY OF THE UTILITY MODEL
Aiming at the defects existing in the prior art, the utility model aims at providing a silver electrolysis anode scrap washing tank.
The purpose of the utility model is realized through the following technical scheme.
The utility model provides a silver electrolysis anode scrap sink, includes the cell body, be equipped with the filtration baffle in the cell body, be equipped with 2 runner tracks on it, the cell body both sides are equipped with bow-shaped splashproof, bow-shaped splashproof is equipped with two buckles, the cell body bottom is equipped with the feed liquid outlet.
The runner track is composed of a track and runners, and the runners are arranged on the track.
The diameter of the rotating wheel is 20mm, and the rotating wheels are densely distributed on the track.
The distance between the filtering baffle and the bottom of the tank body is 150mm to 300mm.
The utility model has the advantages of:
1. the utility model not only has the characteristics of convenient, light and fast washing residual anode, but also has the function of brewing anode mud, and can greatly reduce the labor intensity of post personnel.
2. The utility model discloses rational in infrastructure, easy operation is convenient, strong adaptability, even if women's homophony also can operate, do not choose the people.
3. The utility model is used for wash the anode scrap, save the washing water and be used for soaking and washing anode slime, whole operation reduces this link of pouring liquid, can the using water wisely simultaneously, shortens production cycle, raises the efficiency.
Drawings
Fig. 1 is a schematic structural diagram of the utility model.
Detailed Description
The present invention will be described in detail with reference to the accompanying drawings and specific embodiments.
As shown in fig. 1, a silver electrolysis anode scrap sink comprises a sink body 1, a filtering partition plate 2 is arranged in the sink body 1, 2 runner rails 3 are arranged on the filtering partition plate, bow-shaped splash guards 5 are arranged on two sides of the sink body 1, the bow-shaped splash guards 5 are provided with two buckles 6, and a feed liquid outlet 4 is arranged at the bottom of the sink body 1.
The runner track 3 is composed of a track and runners, and the runners are arranged on the track.
The diameter of the rotating wheel is 15-20mm, and the rotating wheels are densely distributed on the track.
The distance between the filtering baffle plate 2 and the bottom of the tank body 1 is 150mm to 300mm.
Examples
The tank body 1 is a cuboid, the length can be more than twice of the length of the electrolytic tank, the height is more than 30cm of the electrolytic anode scrap, a filtering clapboard 2 is arranged at a position 15cm lower than the lower end of the electrolytic anode scrap, filtering cloth can be laid on the filtering clapboard,
the runner track 3 is fixed on the tank body 1, the runners rotate around fixed shafts and are densely arranged on the track, the smaller the diameter of the runner is, the better the diameter of the runner is, and the materials selected by the runners need to resist pressure and corrosion.
The arched splash-proof baffle 5 is fixed on two sides of the tank body 1 through a rotating shaft, in the process of lifting upwards, the arched splash-proof baffle 5 can rotate along with the shaft, the buckle 6 on the fixed splash-proof baffle 5 is used for buckling, then the splash-proof back baffle is hung behind the arched splash-proof baffle 5, three sides of the washing environment are sealed, a relatively closed operation space is formed, and splashing of feed liquid is prevented.
And a valve is arranged at the feed liquid outlet 4, and after the valve is closed, washing water is replenished to wash the anode mud on the filter cloth to be neutral.
The utility model discloses when using, take off the splashproof backplate earlier, open bow-shaped splashproof backplate 5, filter 2 upper berth filter cloth at the baffle, will be equipped with and wash the crane for the residual anode and place on runner track 3, lift up bow-shaped splashproof backplate 5, hang the splashproof backplate, utilize supporting high-pressure squirt to wash clearly, wash a back clearly, with the residual anode plate of residual anode gin pole one side will be cleared up after one section distance is pulled open forward, wash a residual anode down, after having washed the hanging residual anode, change the splashproof backplate to preceding, recycle high-pressure squirt and residual anode gin pole and wash from the reverse side. After the washing is finished, the splash back baffle is taken down, the arc splash baffle 5 is opened, and the washed anode scrap is arranged in the electrolytic bath by a crane for secondary electrolysis.
When the anode mud accumulated on the filter cloth reaches a certain thickness, the washing water can be supplemented to exceed the anode mud material liquid level on the filter cloth, the anode mud is soaked and washed, the anode mud can be stirred in the soaking and washing process, the washing effect is accelerated, if the end point is not reached in the first washing, the water can be discharged for secondary soaking and washing, and finally the washing end point is reached.
The electrolytic anode scrap is subjected to the operation processes, and the cleaning process of the anode scrap and the cleaning process of the anode mud are completed.
What has been described above is only a preferred embodiment of the present invention, and is not limited to the present invention. It should be noted that other modifications and equivalents may be made by those skilled in the art in light of the teachings of the present disclosure to achieve the same purpose, and should be construed as within the scope of the present disclosure.
Claims (4)
1. The utility model provides a silver electrolysis anode scrap sink, includes the cell body, its characterized in that, be equipped with in cell body (1) and filter baffle (2), be equipped with 2 runner tracks (3) on it, cell body (1) both sides are equipped with bow-shaped splashproof (5), bow-shaped splashproof (5) are equipped with two buckle (6), cell body (1) bottom is equipped with feed liquid outlet (4).
2. The silver electrolysis anode scrap washing tank according to claim 1, wherein the runner track (3) is composed of a track and runners, and the runners are arranged on the track.
3. The silver electrolytic anode scrap washing tank according to claim 2, wherein said runner is 20mm in diameter and densely arranged on the track.
4. The silver electrolysis stub washing tank as claimed in claim 1, wherein the filtering baffle (2) is 150mm to 300mm away from the bottom of the tank body (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220963286.3U CN218610615U (en) | 2022-04-25 | 2022-04-25 | Silver electrolysis residual anode washing tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220963286.3U CN218610615U (en) | 2022-04-25 | 2022-04-25 | Silver electrolysis residual anode washing tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218610615U true CN218610615U (en) | 2023-03-14 |
Family
ID=85422025
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202220963286.3U Active CN218610615U (en) | 2022-04-25 | 2022-04-25 | Silver electrolysis residual anode washing tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218610615U (en) |
-
2022
- 2022-04-25 CN CN202220963286.3U patent/CN218610615U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240409 Address after: 737199 No. 2 Jianshe Road, Jinchuan District, Jinchang City, Gansu Province (east of Beijing Road, west of Heya Road, south of Guiyang Road) Patentee after: Jinchuan Group Copper Gui Co.,Ltd. Country or region after: China Address before: 737100 Beijing Road, Jinchang City, Gansu Province Patentee before: JINCHUAN GROUP Co.,Ltd. Country or region before: China |
|
| TR01 | Transfer of patent right |