CN202116662U - Copper electrolyte purifier - Google Patents
Copper electrolyte purifier Download PDFInfo
- Publication number
- CN202116662U CN202116662U CN2011201921890U CN201120192189U CN202116662U CN 202116662 U CN202116662 U CN 202116662U CN 2011201921890 U CN2011201921890 U CN 2011201921890U CN 201120192189 U CN201120192189 U CN 201120192189U CN 202116662 U CN202116662 U CN 202116662U
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- CN
- China
- Prior art keywords
- tank
- copper
- decoppering
- pipelines
- titanium heat
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- Expired - Fee Related
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- 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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Abstract
The utility model relates to a copper electrolyte purifier, which belongs to the field of wet smelting of copper. The copper electrolyte purifier comprises a collecting tank, a titanium heat exchanger, a circulating pump, an elevated tank, a scalding tank, a decoppering tank, a high-frequency rectifier and a decoppering liquid storage tank. The elevated tank is positioned above the collecting tank and connected with the collecting tank through two pipelines, the circulating pump is arranged on one of the two pipelines, the elevated tank is further respectively connected with the titanium heat exchanger and the decoppering liquid storage tank through pipelines, the titanium heat exchanger and the collecting tank are respectively connected with the decoppering tank through pipelines, the decoppering tank is connected with the scalding tank, and electric wires of the high-frequency rectifier are connected with two ends of the decoppering tank respectively. The copper electrolyte purifier has the advantages of reasonable structural design, fast purifying speed, high efficiency, low manufacturing cost and stable quality.
Description
Technical field
The utility model relates to a kind of cleaning copper electrolyte device, belongs to copper hydrometallurgy field.
Background technology
In copper electrolytic process, detrimental impurity gets into electrolytic solution and constantly rich long-pending through electrochemical dissolution in the blister copper, and impurity behaviors such as As, Sb, Bi will have a strong impact on the cathode copper quality in the electrolytic process.Therefore the timely purifying treatment of copper electrolyte has great significance to ensureing the cathode copper quality in the cathode copper production process.In recent years, because electrolysis raw material anode plate quality fluctuation is bigger, various places supply to contain in the raw material situation of mixing differs, and causes that the electrolytic solution degradation speed speeds in the cathode copper production process.With present state of the art and processing unit, if continue to keep, or the cathode copper product of output does not reach quality standard, or more more renews liquid, causes production cost high, and productivity effect is low.Can not carry out regeneration to sulfuric acid in the electrolytic solution, resource can not get effective comprehensive utilization, and the metal recovery level is not high, and bigger to environment, destruction Of resources property.
The utility model content
The utility model technical problem to be solved provides a kind of reasonable in design, fast, low, the stay-in-grade cleaning copper electrolyte device of efficient high cost of purifying treatment speed.
It is this cleaning copper electrolyte device that the utility model solves the problems of the technologies described above the technical scheme that is adopted; Its constructional feature is: by intercepting basin, titanium heat-exchanger, recycle pump, header tank, scald groove, copper liberation cell, hf rectifier, decopper(ing) liquid storage pool and form; Said header tank is positioned at the intercepting basin top and passes through two pipelines and link to each other with intercepting basin; Wherein a pipeline is provided with recycle pump; Said header tank also links to each other with titanium heat-exchanger, decopper(ing) liquid storage pool respectively through pipeline; Titanium heat-exchanger links to each other with copper liberation cell through pipeline respectively with intercepting basin, copper liberation cell with scald groove and link to each other, the electric wire of said hf rectifier links to each other with the two ends of copper liberation cell respectively.
The described copper liberation cell of the utility model is an integral type with scalding groove.
The utility model is with existing compared with techniques; Have the following advantages and characteristics: the structure production cost of the utility model is low; Productivity effect is high, can carry out regeneration to sulfuric acid in the electrolytic solution, and resource can access effective comprehensive utilization; The metal recovery level is high, and is less to environment, destruction Of resources property.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Label declaration: intercepting basin 1, titanium heat-exchanger 2, recycle pump 3, header tank 4, scald groove 5, copper liberation cell 6, hf rectifier 7, decopper(ing) liquid storage pool 8.
Embodiment
Below in conjunction with embodiment the utility model is done further detailed description, following examples are to the explanation of the utility model and the utility model is not limited to following examples.
Embodiment 1: as shown in Figure 1, the cleaning copper electrolyte device of present embodiment is by intercepting basin 1, titanium heat-exchanger 2, recycle pump 3, header tank 4, scald groove 5, copper liberation cell 6, hf rectifier 7, decopper(ing) liquid storage pool 8 and form.
Header tank 4 is positioned at the top of intercepting basin 1; Header tank 4 passes through two pipelines and links to each other with intercepting basin 1; Wherein a pipeline in the outside is provided with recycle pump 3; Inboard pipeline is that the liquid in the header tank 4 is transported in the intercepting basin 1, and the duct type in the outside is got back to the liquor pump in the intercepting basin 1 in the header tank 4.Said header tank 4 also links to each other with titanium heat-exchanger 2, decopper(ing) liquid storage pool 8 respectively through pipeline; Titanium heat-exchanger 2 links to each other with copper liberation cell 6 through pipeline respectively with intercepting basin 1; Copper liberation cell 6 with scald groove 5 and link to each other and be integral, the electric wire of said hf rectifier 7 links to each other with the two ends of copper liberation cell 6 respectively.
In addition, need to prove, the specific embodiment described in this specification sheets, its zero, the shape of parts, institute's title of being named etc. can be different.Allly conceive equivalence or the simple change that described structure, characteristic and principle are done, include in the protection domain of the utility model patent according to the utility model patent.The utility model person of ordinary skill in the field can make various modifications or replenishes or adopt similar mode to substitute described specific embodiment; Only otherwise depart from the structure of the utility model or surmount the defined scope of these claims, all should belong to the protection domain of the utility model.
Claims (2)
1. cleaning copper electrolyte device; It is characterized in that: by intercepting basin, titanium heat-exchanger, recycle pump, header tank, scald groove, copper liberation cell, hf rectifier, decopper(ing) liquid storage pool and form; Said header tank is positioned at the intercepting basin top and passes through two pipelines and link to each other with intercepting basin; Wherein a pipeline is provided with recycle pump, and said header tank also links to each other with titanium heat-exchanger, decopper(ing) liquid storage pool respectively through pipeline, and titanium heat-exchanger links to each other with copper liberation cell through pipeline respectively with intercepting basin; Copper liberation cell with scald groove and link to each other, the electric wire of said hf rectifier links to each other with the two ends of copper liberation cell respectively.
2. cleaning copper electrolyte device according to claim 1 is characterized in that: described copper liberation cell is an integral type with scalding groove.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201921890U CN202116662U (en) | 2011-06-09 | 2011-06-09 | Copper electrolyte purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201921890U CN202116662U (en) | 2011-06-09 | 2011-06-09 | Copper electrolyte purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202116662U true CN202116662U (en) | 2012-01-18 |
Family
ID=45457743
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201921890U Expired - Fee Related CN202116662U (en) | 2011-06-09 | 2011-06-09 | Copper electrolyte purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202116662U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103469255A (en) * | 2013-09-09 | 2013-12-25 | 梧州漓佳铜棒有限公司 | Device and method for recycling copper anode plate soaking liquid |
| CN103526230A (en) * | 2013-10-08 | 2014-01-22 | 铜陵有色金属集团股份有限公司金昌冶炼厂 | Method for producing high-quality cathode copper with high efficiency in copper electrolyte purification process |
| CN103572321A (en) * | 2013-11-18 | 2014-02-12 | 梧州漓佳铜棒有限公司 | Copper removing device and method for electrolyte |
| CN106498440A (en) * | 2016-12-13 | 2017-03-15 | 云南锡业股份有限公司铜业分公司 | A kind of copper electrolysis system fluid balance control method |
| CN111254463A (en) * | 2020-03-10 | 2020-06-09 | 吉林紫金铜业有限公司 | Decoppering system |
-
2011
- 2011-06-09 CN CN2011201921890U patent/CN202116662U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103469255A (en) * | 2013-09-09 | 2013-12-25 | 梧州漓佳铜棒有限公司 | Device and method for recycling copper anode plate soaking liquid |
| CN103469255B (en) * | 2013-09-09 | 2015-12-23 | 重庆潼双机械制造有限公司 | The recycling device of copper anode plate foam washing liquid and method |
| CN103526230A (en) * | 2013-10-08 | 2014-01-22 | 铜陵有色金属集团股份有限公司金昌冶炼厂 | Method for producing high-quality cathode copper with high efficiency in copper electrolyte purification process |
| CN103526230B (en) * | 2013-10-08 | 2015-12-09 | 铜陵有色金属集团股份有限公司金昌冶炼厂 | A kind of method of cleaning copper electrolyte processing efficient production high-quality cathode copper |
| CN103572321A (en) * | 2013-11-18 | 2014-02-12 | 梧州漓佳铜棒有限公司 | Copper removing device and method for electrolyte |
| CN106498440A (en) * | 2016-12-13 | 2017-03-15 | 云南锡业股份有限公司铜业分公司 | A kind of copper electrolysis system fluid balance control method |
| CN106498440B (en) * | 2016-12-13 | 2018-04-03 | 云南锡业股份有限公司铜业分公司 | A kind of copper electrolysis system fluid balance control method |
| CN111254463A (en) * | 2020-03-10 | 2020-06-09 | 吉林紫金铜业有限公司 | Decoppering system |
| CN111254463B (en) * | 2020-03-10 | 2021-05-04 | 吉林紫金铜业有限公司 | Decoppering system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120118 Termination date: 20130609 |