CN210065949U - Ultrathin anode plate - Google Patents
Ultrathin anode plate Download PDFInfo
- Publication number
- CN210065949U CN210065949U CN201822044551.4U CN201822044551U CN210065949U CN 210065949 U CN210065949 U CN 210065949U CN 201822044551 U CN201822044551 U CN 201822044551U CN 210065949 U CN210065949 U CN 210065949U
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- anode plate
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Abstract
The utility model relates to an ultra-thin anode plate. The anode plate is positioned between the two reticular support frames, and the two reticular support frames are fixedly connected through the embedded ribs. The utility model discloses reduce by a wide margin with lead-based alloy material, but anode plate alloy plate thickness attenuate is 1-4 mm, plastics, the embedded two-sided netted parcel support chassis of non-metallic material preparation such as epoxy makes novel ultra-thin anode plate face have better hardness than traditional thick face anode plate, and is more difficult bending deformation, is more difficult for taking place the short circuit with the cathode plate in process of production and burns the board phenomenon.
Description
The technical field is as follows:
the utility model relates to an ultra-thin anode plate.
Background art:
as is known, the metal is smelted to produce basic metal raw material products, there are two important technological modes of pyrometallurgy and hydrometallurgy at present, the hydrometallurgy is generally the process of leaching the raw material containing minerals such as copper, zinc, etc. with acidic or alkaline solution, adopting leaching mode, then extracting, enriching, and electrodepositing production, and the electrodepositing process is that insoluble conductive anode and cathode of the starting sheet (cathode plate) are arranged in the electrolytic bath, under the action of direct current, the metal cation called as the electrolyte in the electrolytic bath after being enriched is separated out to the cathode of the starting sheet (cathode plate), and the required products such as electrodeposited copper and electrodeposited zinc, etc. are produced, and the insoluble lead alloy anode plate is used as the durable conductive electrode, fixed and used for a long time in the electrolytic bath, and is also the main body of product cost consumption. In the period, the manufacturing cost and the electric conductivity of the anode plate and the yield of the anode plate and the cathode plate precipitation products play a vital role in every ton of electricity consumption of the products.
The current wet-process metallurgical technology is most widely applied, the wet-process electro-deposition copper and the wet-process electro-deposition zinc with super large product scale are produced, the annual output of the two metal varieties, namely Chilean and American wet-process electro-deposition copper, is 200 ten thousand tons in 1989, about 6 ten thousand tons in China at present, the annual output of the wet-process electro-zinc is nearly ten thousand tons in the whole world, the annual output of the wet-process electro-zinc is over 400 ten thousand tons in China, and the annual output of the wet-process electro-zinc is nearly 100 ten thousand tons in only Yunnan. In the two metal varieties, the current efforts of various electrode technology enterprises for saving electricity and reducing cost of the anode plate are concentrated on the aspects of addition of elements such as silver, calcium, strontium, rare earth and the like and plate-shaped rolling technologies. The metal hardness and the crystallization compactness of the anode plate are improved, and the effects of saving electricity and reducing the cost are achieved, but the problem of greatly reducing the material consumption of the anode plate is not fundamentally solved.
The utility model has the following contents:
the utility model discloses just to above-mentioned problem, provide an ultra-thin anode plate.
In order to realize the above purpose, the utility model discloses a following technical scheme, including anode plate, two netted support frames and embedding rib, the anode plate is located between two netted support frames, through embedding rib fixed connection between two netted support frames.
The anode plate is formed by rolling lead and lead-based alloy, and the support frame is made of plastic, plastic or epoxy resin.
The net-shaped support frame is formed by arranging support rods in a net shape.
The thickness of the anode plate is 1-4 mm.
The utility model has the advantages that:
the utility model discloses reduce by a wide margin with lead-based alloy material, but anode plate alloy plate thickness attenuate is 1-4 mm, plastics, the embedded two-sided netted parcel supporting framework of non-metallic material preparation such as epoxy, make novel ultra-thin anode plate face have better hardness than traditional thick plate face anode plate, more difficult bending deformation, more difficult short circuit takes place to burn the board phenomenon with the cathode plate in process of production, especially the face is long-pending > 1.6 big board more than the square meter, economize on electricity, the material saving effect is better.
Description of the drawings:
fig. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a side view of fig. 1.
In the figure, 1 is a net-shaped support frame, 2 is an embedded rib, and 3 is an anode plate.
The specific implementation mode is as follows:
as can be seen from the figures 1-2, the utility model comprises an anode plate, two netted supporting frames and an embedded rib, wherein the anode plate is positioned between the two netted supporting frames, and the two netted supporting frames are fixedly connected through the embedded rib.
The anode plate is formed by rolling lead and lead-based alloy, and the support frame is made of plastic, plastic or epoxy resin.
The net-shaped support frame is formed by arranging support rods in a net shape.
The thickness of the anode plate is 1-4 mm.
The top of the anode plate is provided with a copper beam and a lifting lug.
The two reticular support frames and the anode plate are bonded and fixed through epoxy resin.
When copper is electrodeposited or zinc is electrolyzed, an anode plate and a cathode plate which meet the specification of the electrolytic cell are placed together, an electrolytic cell of a direct current power supply system such as a conductive copper bar and the like is prepared, acidic copper-rich liquid containing copper ions of more than or equal to 20 g/l and zinc-rich liquid containing zinc ions of more than or equal to 50 g/l are pumped, after electrification, under the action of strong current, current passes through a conductive electrode of the anode plate, if the electrolytic copper is electrodeposited, the copper ions are separated out from the cathode and attached to a starting plate (the cathode plate), the electro-rich liquid containing the copper ions is reduced, the electro-rich liquid enters an extraction enrichment cycle and then enters the electrolytic cell, and the production of the electrodeposited copper is completed in a certain period; if the electrolytic deposition of zinc is carried out, zinc ions are separated out from the cathode and attached to the cathode plate, so that zinc-rich liquid with reduced zinc ions enters leaching, filtering, clarifying and enriching circulation, then the zinc-rich liquid enters an electrolytic bath, is stripped from the cathode plate after a certain period, is melted into ingots to complete the production of electrolytic zinc, and if other metals are electrodeposited, the zinc-rich liquid is also separated out from a starting sheet (cathode plate) to complete the production process of metal products produced by electrodeposition electrolysis.
The above embodiments are preferred embodiments of the present invention, but the present invention is not limited to the above embodiments, and any other modifications, applications, and simplifications made by the manufacturing process of the embedded net, the thickness structure of the plate material should be replaced by equivalent ones, and all such modifications, applications, and simplifications are included in the protection scope of the present invention.
Claims (2)
1. The ultrathin anode plate is characterized by comprising an anode plate, two net-shaped supporting frames and embedded ribs, wherein the anode plate is positioned between the two net-shaped supporting frames, the two net-shaped supporting frames are fixedly connected through the embedded ribs, the anode plate is formed by rolling lead and lead-based alloy, the supporting frames are made of plastic, plastic or epoxy resin, and the net-shaped supporting frames are formed by supporting rods in a net-shaped arrangement mode.
2. The ultra-thin anode plate of claim 1, wherein the thickness of the anode plate is 1-4 mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822044551.4U CN210065949U (en) | 2018-12-07 | 2018-12-07 | Ultrathin anode plate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822044551.4U CN210065949U (en) | 2018-12-07 | 2018-12-07 | Ultrathin anode plate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210065949U true CN210065949U (en) | 2020-02-14 |
Family
ID=69424211
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822044551.4U Expired - Fee Related CN210065949U (en) | 2018-12-07 | 2018-12-07 | Ultrathin anode plate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210065949U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111876794A (en) * | 2020-07-20 | 2020-11-03 | 有研粉末新材料股份有限公司 | Negative plate combined structure, electrolysis device and copper powder preparation method |
-
2018
- 2018-12-07 CN CN201822044551.4U patent/CN210065949U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111876794A (en) * | 2020-07-20 | 2020-11-03 | 有研粉末新材料股份有限公司 | Negative plate combined structure, electrolysis device and copper powder preparation method |
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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: 20200214 Termination date: 20211207 |