CN103103557A - Novel electrolytic bath - Google Patents
Novel electrolytic bath Download PDFInfo
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- CN103103557A CN103103557A CN 201210527348 CN201210527348A CN103103557A CN 103103557 A CN103103557 A CN 103103557A CN 201210527348 CN201210527348 CN 201210527348 CN 201210527348 A CN201210527348 A CN 201210527348A CN 103103557 A CN103103557 A CN 103103557A
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- hole
- discharge port
- chamber
- cell body
- electrolytic bath
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Abstract
The invention discloses a novel electrolytic bath which comprises a bath body, wherein a baffle plate is arranged in the bath body to divide the bath body into a first chamber and a second chamber; the second chamber is near to the bottom of the bath body; a through hole is formed on the baffle plate; the diameter of the through hole is greater than that of an anode slime particle; a discharge port is formed on the bath body; and a water suction pump is connected to the discharge port. According to the electrolytic bath, the through hole is formed on the baffle plate; and the diameter of the through hole is greater than that of the anode slime particle, so that the slime particle is allowed to pass through the through hole, and a large blister copper is prevented from passing through the through hole to block the discharge port. In addition, the water suction pump is connected to the discharge port, so that the anode slime in the second chamber can be easily sucked out, i.e., the operation that the anode slime is manually removed from the electrolytic bath bit by bit with production stopping is not required. Therefore, the production efficiency is improved.
Description
Technical field
The invention belongs to the technical field of electrolyzer, relate in particular to a kind of novel electrolytic bath.
Background technology
Electrolyzer is electrolytical storage tanks, when electrolytic copper, blister copper (cupric 99%) is made slab in advance as anode, and the pure copper flakiness is made negative electrode, with the mixed liquid of sulfuric acid (H2SO4) and copper sulfate (CuSO4) as electrolytic solution.After energising, copper becomes cupric ion (Cu) to movable cathode from anode dissolution, arrives electron gain after negative electrode and separates out fine copper (also claiming electrolytic copper) at negative electrode.In blister copper, impurity is dissolved as ion (Zn and Fe) as meetings such as the iron that sprinkles than work in copper and zinc with copper.Compare with cupric ion due to these ions and be difficult for separating out, so can avoid these ions to separate out on anode as long as suitably regulate potential difference during electrolysis.Be deposited on the bottom of electrolyzer as gold and silver etc. than the inactive impurity of copper.The copper coin of producing like this is called " electrolytic copper ", and quality is high, can be used for making electric product.Be deposited in be called " anode sludge " of bottom of electrolytic tank, gold and silver is rich in the inside, is very valuable, and taking out reprocessing has high economic worth.
The anode sludge reclaims needs very large workload, and present mud collection needs to stop production by manually bit by bit removing in groove, and is not only time-consuming, and causes the parking underproduction, reduced production efficiency, increased cost.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of novel electrolytic bath that can better collect the anode sludge.
In order to solve the problems of the technologies described above, the invention provides following technical scheme: a kind of novel electrolytic bath, comprise cell body, being provided with dividing plate in cell body, is the first chamber and the second chamber with the cell body horizontal subdivision, and the second chamber is near the cell body bottom, have through hole on dividing plate, through-hole diameter is greater than the diameter of anode sludge particle, and cell body is provided with discharge port, connects lift pump on discharge port.
Compared with prior art, the invention has the advantages that: have through hole on dividing plate, through-hole diameter is greater than the diameter of anode sludge particle, can allow mud pellet to pass through, also prevent that the blister copper of bulk from passing through through hole simultaneously, avoid the obstruction discharge port, connect lift pump on discharge port, can not need to stop production by manually bit by bit removing in groove like a cork with the anode sludge sucking-off in the second chamber, improved production efficiency.
Further, described discharge port is positioned at the bottom of cell body, also is deposited in the bottom of cell body because of the anode sludge, therefore the sucking-off anode sludge preferably.
Description of drawings
Below in conjunction with drawings and Examples, technical solution of the present invention is further illustrated:
Fig. 1 is the structural representation of novel electrolytic bath embodiment of the present invention.
Embodiment
As shown in Figure 1, a kind of novel electrolytic bath of the present invention, comprise cell body 1, being provided with dividing plate 2 in cell body 1, is the first chamber and the second chamber with cell body 1 horizontal subdivision, and the second chamber is near cell body 1 bottom, have through hole on dividing plate 2, through-hole diameter is greater than the diameter of anode sludge particle, and cell body 1 is provided with discharge port 3, connects lift pump 4 on discharge port 3.Described discharge port 3 is positioned at the bottom of cell body 1, also is deposited in the bottom of cell body 1 because of the anode sludge, therefore the sucking-off anode sludge preferably.
Have through hole on dividing plate 2 of the present invention, through-hole diameter is greater than the diameter of anode sludge particle, can allow mud pellet to pass through, simultaneously prevented that also the blister copper of bulk from passing through through hole, avoid obstruction discharge port 3, connected lift pump 4 on discharge port 3, can be like a cork with the anode sludge sucking-off in the second chamber, do not need to stop production by manually bit by bit removing in groove, improved production efficiency.
For a person skilled in the art, under the prerequisite that does not break away from structure of the present invention, can also make some distortion and improvement, these also should be considered as protection scope of the present invention, and these can not affect effect of the invention process and practical applicability.
Claims (2)
1. novel electrolytic bath, comprise cell body, be characterised in that: be provided with dividing plate in cell body, be the first chamber and the second chamber with the cell body horizontal subdivision, the second chamber has through hole near the cell body bottom on dividing plate, through-hole diameter is greater than the diameter of anode sludge particle, cell body is provided with discharge port, connects lift pump on discharge port.
2. novel electrolytic bath as claimed in claim 1, it is characterized in that: described discharge port is positioned at the bottom of cell body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201210527348 CN103103557A (en) | 2012-12-10 | 2012-12-10 | Novel electrolytic bath |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201210527348 CN103103557A (en) | 2012-12-10 | 2012-12-10 | Novel electrolytic bath |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103103557A true CN103103557A (en) | 2013-05-15 |
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ID=48311739
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201210527348 Pending CN103103557A (en) | 2012-12-10 | 2012-12-10 | Novel electrolytic bath |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103103557A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104562066A (en) * | 2015-01-20 | 2015-04-29 | 昆山美源达环保科技有限公司 | Acid copper sulfate vortex electrolysis system |
-
2012
- 2012-12-10 CN CN 201210527348 patent/CN103103557A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104562066A (en) * | 2015-01-20 | 2015-04-29 | 昆山美源达环保科技有限公司 | Acid copper sulfate vortex electrolysis system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20130515 |