CN202989297U - Electrolytic metal production line by wet method - Google Patents
Electrolytic metal production line by wet method Download PDFInfo
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- CN202989297U CN202989297U CN2012207451821U CN201220745182U CN202989297U CN 202989297 U CN202989297 U CN 202989297U CN 2012207451821 U CN2012207451821 U CN 2012207451821U CN 201220745182 U CN201220745182 U CN 201220745182U CN 202989297 U CN202989297 U CN 202989297U
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- electrolytic
- production line
- electrolytic cells
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- metal production
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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 discloses an electrolytic metal production line by a wet method. The electrolytic metal production line comprises a plurality of electrolytic cells which are divided into two groups, wherein one group of electrolytic cells is connected with the positive electrode of rectifying equipment, and the other group of electrolytic cells is connected with the negative electrode of rectifying equipment, and the two groups are connected in series; and the electrolytic cells in each group are connected in parallel. A loop current is improved by increasing the number of the electrolytic cells connected in parallel in a single group, while the number of the electrolytic cells connected in series is not increased, i.e., a loop voltage is not increased, so that the safety problem of rise of an electrolytic loop voltage is solved, and the problems of high power consumption and irregular electrolysis caused by nonuniform rich and poor cations due to extension of the electrolytic cells are solved as well; and meanwhile, the nonstandard design method that one transformer is used by two production lines is avoided, and the problem of high scrap iron loss of the transformer brought by production halt when one of the two production lines goes wrong is also solved, and thus the electrolytic metal production line has the advantages of high productivity and safety production.
Description
Technical field
The utility model relates to a kind of wet method electrolysis Metal Production line, particularly a kind of wet method electrolysis Metal Production line that can improve the single line production capacity.
Background technology
Electrolytic metal Mn and other electrolysis industries, past is all the design that adopts also, connect and combine, and is exactly with the moon in an electrolyzer, positive plate is distinguished parallel connection, then several electrolyzers are connected into an electrolysis loop.With this method of design, just can only adopt dual mode if increase wall scroll production line industrial scale, first kind of way is that the quantity increasing strength of current that increases yin, yang pole plate in parallel in electrolyzer reaches the requirement that improves production capacity; The second way is to increase the quantity of electrolyzer by strengthening the voltage in electrolysis loop, reaches the requirement that improves production capacity.But all have problems by this dual mode: the one, electrolyzer is oversize, Mn in groove
2+The concentration of ion, rich or poor differ too greatly produce unfavorablely to electrolysis, can produce energy consumption; The 2nd, electrolyzer is too many, and loop voltage is too high easily to cause the accident, dangerous.Therefore, in recent years must be through reaching 10000 tons due to the wall scroll production line scale of national regulation industry access policy requirements electrolytic manganese.All adopt two low voltage outlet terminals of a rectifier transformer design in industry, the electrolytic manganese production line mode that drives two 5000 tons is dealt with the industry access Policy Conditions.Can this design have problems equally: if any wherein a production line is out of joint, and another production line is being produced, and will produce the transformer fe expense loss of great number, has wasted the energy, has improved cost.
The utility model content
The purpose of this utility model is to provide a kind of wet method electrolysis Metal Production line of safe, high production capacity.
This wet method electrolysis Metal Production line that the utility model provides comprises some electrolyzers, and they are divided into two groups, and one group is connected with the positive pole of rectifying installation, and another group is connected with the negative pole of rectifying installation, connects between two groups; Parallel with one another between each electrolyzer of described each group.
The utility model improves the electric current in loop by increasing single group electrolyzer quantity in parallel, and does not increase the electrolyzer quantity of series connection, does not namely improve the voltage in loop.So not only solve the safety problem that the electrolysis loop voltage raises, solved again the problem that electrolysis is undesired, power consumption is high that causes the metallic cation too much difference between the rich and the poor to cause owing to lengthening electrolyzer.Overcome simultaneously a transformer and dragged two this nonstandard method of design of production line, also having solved wherein, a production line goes wrong stopping production and brings the problem of the transformer fe expense loss of great number.Thereby the advantage with high production capacity and safety in production.
Description of drawings
Fig. 1 is that a preferred embodiment of the present utility model is overlooked connection diagram.
Embodiment
As shown in Figure 1, this wet method electrolysis Metal Production line with the utility model provides is used for electrolytic manganese.It comprises some electrolyzers 1, and they are divided into two groups, and one group is connected with the positive pole of rectifying installation, and another group is connected with the negative pole of rectifying installation, connects between two groups; Parallel with one another by conductive bus bar 2 between each electrolyzer 1 of each group.Be connection busbar 3 series connection of conductive bus bar 2 length twices by length between two groups of electrolyzers.Facts have proved, electrolyzer adopts mode of connection of the present utility model, can make the scale of wall scroll electrolytic manganese production line can reach 1-3 more than ten thousand tons.
Claims (1)
1. a wet method electrolysis Metal Production line, comprise some electrolyzers, it is characterized in that: described electrolyzer is divided into two groups, and one group is connected with the positive pole of rectifying installation, and another group is connected with the negative pole of rectifying installation, connects between two groups; Parallel with one another between each electrolyzer of each group.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012207451821U CN202989297U (en) | 2012-12-31 | 2012-12-31 | Electrolytic metal production line by wet method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012207451821U CN202989297U (en) | 2012-12-31 | 2012-12-31 | Electrolytic metal production line by wet method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202989297U true CN202989297U (en) | 2013-06-12 |
Family
ID=48560493
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012207451821U Expired - Fee Related CN202989297U (en) | 2012-12-31 | 2012-12-31 | Electrolytic metal production line by wet method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202989297U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105063661A (en) * | 2015-08-29 | 2015-11-18 | 王兆兵 | Wet method electrolytic metal full-automatic production system |
-
2012
- 2012-12-31 CN CN2012207451821U patent/CN202989297U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105063661A (en) * | 2015-08-29 | 2015-11-18 | 王兆兵 | Wet method electrolytic metal full-automatic production system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130612 Termination date: 20171231 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |