CN210215572U - Production equipment for silver electrolysis - Google Patents
Production equipment for silver electrolysis Download PDFInfo
- Publication number
- CN210215572U CN210215572U CN201921155301.6U CN201921155301U CN210215572U CN 210215572 U CN210215572 U CN 210215572U CN 201921155301 U CN201921155301 U CN 201921155301U CN 210215572 U CN210215572 U CN 210215572U
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- Prior art keywords
- communicated
- outlet
- circulating
- tee joint
- silver
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- Expired - Fee Related
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- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 title claims abstract description 31
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 25
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 22
- 229910052709 silver Inorganic materials 0.000 title claims abstract description 22
- 239000004332 silver Substances 0.000 title claims abstract description 22
- 238000010079 rubber tapping Methods 0.000 claims abstract description 14
- 239000000428 dust Substances 0.000 claims description 9
- 239000004744 fabric Substances 0.000 claims description 8
- 238000007599 discharging Methods 0.000 abstract description 2
- 238000004140 cleaning Methods 0.000 abstract 1
- 210000004027 cell Anatomy 0.000 description 25
- 239000000463 material Substances 0.000 description 11
- 239000003792 electrolyte Substances 0.000 description 6
- 210000003040 circulating cell Anatomy 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 235000013361 beverage Nutrition 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
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- Electrolytic Production Of Metals (AREA)
Abstract
The utility model provides a production facility for silver electrolysis, which comprises an electrolytic bath, a circulating bath and a circulating pump, wherein the bottom of the electrolytic bath is provided with a tee joint, the inlet of the tee joint is communicated with the outlet at the bottom of the electrolytic bath, one outlet of the tee joint is communicated with the top of the circulating bath through a tapping valve, and the other outlet of the tee joint is provided with a discharging valve; the inlet of the circulating pump is communicated with the bottom of one side of the circulating tank, and the outlet of the circulating pump is communicated with the electrolytic tank. The production equipment for silver electrolysis has the advantages of convenient cleaning and high efficiency.
Description
Technical Field
The utility model relates to a production facility for silver electrolysis.
Background
The silver electrolytic cell is the equipment of producing silver through the mode of electrolysis, adopts horizontal electrolytic cell at present mostly, carries the silver powder of production out of the electrolytic cell through the mode of belt transport, for example the silver electrolytic cell that discloses in the patent document with application number 201520589231.0, contains the sub-groove of a plurality of bottoms UNICOM in the electrolytic cell, is equipped with belt conveyor system at the bottom of the electrolytic cell groove, and the one end design of electrolytic cell is slope formula, and the conveyor belt extends to outside the groove along the slope. Silver powder separated out from the negative plate falls onto the conveying belt during electrolysis, and the belt conveying system is started to take the silver powder out of the electrolytic tank. However, the belt conveying mode of the horizontal electrolytic cell has the following defects: after the silver powder is taken out of the end of the electrolytic cell by the conveying belt, the silver powder on the belt cannot be completely unloaded into the material receiving trolley, and the silver powder remaining on the belt returns to the electrolytic cell along with the belt and falls on the bottom of the electrolytic cell below the conveying belt. The silver powder accumulated on the bottom of the cell can affect the operation of the belt system after accumulating to a certain degree, so that the belt system needs to be disassembled to clean the silver powder accumulated below when the electrolytic production is stopped, which is time-consuming and labor-consuming.
Disclosure of Invention
In order to solve the problems existing in the background technology, the utility model provides a production device for silver electrolysis.
A production device for silver electrolysis comprises an electrolytic cell, a circulating cell and a circulating pump, wherein a tee joint is arranged at the bottom of the electrolytic cell, an inlet of the tee joint is communicated with an outlet at the bottom of the electrolytic cell, one outlet of the tee joint is communicated with the top of the circulating cell through a tapping valve, and a tapping valve is arranged at the other outlet of the tee joint; the inlet of the circulating pump is communicated with the bottom of one side of the circulating tank, and the outlet of the circulating pump is communicated with the electrolytic tank.
Based on the above, the lower part of the electrolytic cell is funnel-shaped, and the outlet at the bottom of the electrolytic cell is arranged at the bottommost part of the funnel-shaped structure.
Based on the above, the tee joint is communicated with the outlet of the circulating groove and is provided with a filter screen.
Based on the above, the upper part of the circulation groove is provided with the filter disc, and the filter disc is laid with the filter cloth.
Based on the above, the upper part of one side of the electrolytic cell is provided with the overflow port, and the overflow port is communicated with the top of the circulating tank.
Based on the above, still include the dust cover, the dust cover passes through flange joint in the exit of baiting valve.
The utility model discloses relative prior art has substantive characteristics and progress, specific theory, the utility model discloses changed ejection of compact mode, discharged electrolyte after the electrolysis production, emit the back with silver powder through the baiting valve again, carry back the electrolysis trough through the circulating pump with electrolyte and carry out cyclic utilization, and need not belt transport structure in the electrolysis trough, need not too much dismouting work when clearing up the electrolysis trough, the clearance work is more convenient, efficiency is higher.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
Fig. 1 is a schematic structural diagram of the present invention.
In the figure: 1. an electrolytic cell; 2. a circulation tank; 3. a circulation pump; 4. a tee joint; 5. a tapping valve; 6. a discharge valve; 7. a filter disc; 8. an overflow port; 9. a dust cover.
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 any creative effort belong to the protection scope of the present invention.
As shown in fig. 1, a production apparatus for silver electrolysis comprises an electrolytic cell 1, a circulation cell 2 and a circulation pump 3, wherein a tee joint 4 is arranged at the bottom of the electrolytic cell 1, an inlet of the tee joint 4 is communicated with an outlet at the bottom of the electrolytic cell 1, one outlet of the tee joint 4 is communicated with the top of the circulation cell 2 through a tapping valve 5, and a tapping valve 6 is arranged at the other outlet of the tee joint 4; the inlet of the circulating pump 3 is communicated with the bottom of one side of the circulating tank 2, and the outlet of the circulating pump 3 is communicated with the electrolytic tank 1.
During production, the tapping valve 5 and the discharge valve 6 are respectively closed. When the production is finished, the tapping valve 5 is opened firstly, and the electrolyte enters the circulating tank 2 for temporary storage through the tapping valve 5 and the pipeline. After the tapping, close bleeder valve 5 and open bleeder valve 6, gather the silver-colored material in 1 bottom of electrolysis trough and can be emitted by bleeder valve 6 department, place the skip car that connects in the reality below the bleeder valve 6 and connect the material, and owing to carried out electrolyte tapping operation earlier, the content of electrolyte is less in the silver-colored material, conveniently washes the silver-colored material. In this embodiment, the lower part of electrolysis trough 1 is for leaking hopper-shaped, the export setting of electrolysis trough 1 bottom is at the bottommost of leaking hopper-shaped structure, and the convenient silver material of producing of structure that leaks hopper-shaped gathers to the export in electrolysis trough 1 bottom, conveniently arranges the material.
Preferably, tee bend 4 intercommunication the exit of circulation groove 2 is provided with the filter screen, filters the silver-colored material when carrying out the tapping operation, avoids the beverage to get into in the circulation groove 2. In this embodiment, the filter screen is a stainless steel filter screen of 100 meshes, and the diameter of each mesh of the filter holes is 0.15 mm. In practice, an overflow port 8 is formed in the upper portion of one side of the electrolytic cell 1, the overflow port 8 is communicated with the top of the circulation tank 2, and a 100-mesh filter screen is also arranged at the overflow port 8 in practice.
Preferably, a filter disc 7 is arranged at the upper part of the circulation tank 2, filter cloth is laid on the filter disc 7, and the electrolyte entering the circulation tank 2 from the drain valve 5 and the overflow port 8 is filtered by the filter cloth on the filter disc 7 and then enters the circulation tank 2. In practice, the filter cloth plays a role in checking the filtering effect of the filter screen, silver materials are filtered by the filter screen under normal conditions, and no silver materials are filtered out of the filter cloth; if silver materials on the filter cloth are filtered out, the problem of filtering at the filter screen is solved, and the filter cloth needs to be checked and repaired.
Preferably, the production equipment for silver electrolysis further comprises a dust cover 9, wherein the dust cover 9 is connected to the outlet of the discharge valve 6 through a flange, and the discharge pipeline is protected from dust during normal production, so that the pipeline is prevented from being polluted. When the production is finished, the dust cover 9 is firstly dismounted, and then the discharging operation is carried out.
It is obvious to a person skilled in the art that the invention is not restricted to details of the above-described exemplary embodiments, but that it can be implemented in other specific forms without departing from the spirit or essential characteristics of the invention. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Claims (6)
1. A production facility for silver electrolysis, characterized in that: the electrolytic bath device comprises an electrolytic bath, a circulating bath and a circulating pump, wherein a tee joint is arranged at the bottom of the electrolytic bath, an inlet of the tee joint is communicated with an outlet at the bottom of the electrolytic bath, one outlet of the tee joint is communicated with the top of the circulating bath through a tapping valve, and a tapping valve is arranged at the other outlet of the tee joint; the inlet of the circulating pump is communicated with the bottom of one side of the circulating tank, and the outlet of the circulating pump is communicated with the electrolytic tank.
2. The production plant for silver electrolysis according to claim 1, characterized in that: the lower part of the electrolytic cell is funnel-shaped, and an outlet at the bottom of the electrolytic cell is arranged at the bottommost part of the funnel-shaped structure.
3. The production plant for silver electrolysis according to claim 1, characterized in that: and a filter screen is arranged at an outlet of the tee joint communicated with the circulating groove.
4. The production plant for silver electrolysis according to claim 1, characterized in that: and a filter disc is arranged at the upper part of the circulating groove, and filter cloth is laid on the filter disc.
5. The production plant for silver electrolysis according to claim 1, characterized in that: an overflow port is formed in the upper portion of one side of the electrolytic cell and communicated with the top of the circulating tank.
6. The production plant for silver electrolysis according to claim 1, characterized in that: still include the dust cover, the dust cover passes through flange joint in the exit of baiting valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921155301.6U CN210215572U (en) | 2019-07-22 | 2019-07-22 | Production equipment for silver electrolysis |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921155301.6U CN210215572U (en) | 2019-07-22 | 2019-07-22 | Production equipment for silver electrolysis |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210215572U true CN210215572U (en) | 2020-03-31 |
Family
ID=69917501
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921155301.6U Expired - Fee Related CN210215572U (en) | 2019-07-22 | 2019-07-22 | Production equipment for silver electrolysis |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210215572U (en) |
-
2019
- 2019-07-22 CN CN201921155301.6U patent/CN210215572U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200331 |