CN204162803U - The lead electrolytic solution recycle system - Google Patents
The lead electrolytic solution recycle system Download PDFInfo
- Publication number
- CN204162803U CN204162803U CN201420492152.3U CN201420492152U CN204162803U CN 204162803 U CN204162803 U CN 204162803U CN 201420492152 U CN201420492152 U CN 201420492152U CN 204162803 U CN204162803 U CN 204162803U
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- China
- Prior art keywords
- electrolytic solution
- cyclic acid
- annular seal
- acid pump
- seal space
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Abstract
The utility model discloses a kind of electrolytic solution reservoir, cyclic acid pump and electrolyzer, also comprise electrolytic solution and retain annular seal space, described electrolytic solution retains annular seal space and to be placed in above electrolytic solution reservoir and electrolytic solution retains annular seal space inner top is provided with into pipe, and this entrance entering pipe is placed in electrolytic solution reservoir electrolytic solution; Described electrolytic solution to retain in annular seal space liquid level higher than cyclic acid pump entrance and electrolytic solution retain bottom annular seal space with cyclic acid pump entrance UNICOM, make electrolytic solution retain in annular seal space and cyclic acid pump internal memory leaves electrolytic solution; Described cyclic acid pump outlet and electrolyzer UNICOM.Without the need at cyclic acid pump portal perfusion electrolytic solution during startup cyclic acid pump, directly turn on the power switch, easy to use, long service life, simple to operate.
Description
Technical field
The utility model relates to a kind of metal electrolysis means, particularly a kind of lead electrolytic solution recycle system.
Background technology
When plumbous electrolysis, electrolytic solution does not stop to circulate.At present, the lead electrolytic solution circulation device of employing, generally comprises electrolysis liquid pool, sour pump and electrolyzer.Its working process is: the electrolytic solution in electrolysis liquid pool is pumped in electrolyzer, again by sour pump and flowed in electrolyzer by the outlet of electrolyzer, does not stop to circulate.In actual use, in order to keep the safety in production, the electrolysis liquid pool of lead electrolytic solution circulation device is arranged at below ground, and electrolyzer is arranged at more than ground, has height fall between electrolysis liquid pool and electrolyzer, so adopt sour pump to be pumped in electrolyzer by electrolytic solution.Because electrolytic solution is acid solution, have extremely strong corrodibility, sour pump can not directly be placed in electrolysis liquid pool, must by pipeline and electrolysis liquid pool inline logical.
When sour pump is placed on ground, before sour pump startup, electrolysis liquid pool electrolyte inside must could be pumped into electrolyzer at sour pump intake perfusion electrolytic solution.In the process of sour pump intake perfusion electrolytic solution, must two people's tacit agreement cooperations just can complete, inefficiency, uses inconvenience.
When sour pump is placed in below ground, need to build a pump pond in underground, make sour pump lower than electrolysis liquid pool electrolyte inside face.In actual use, sour pump discharge, entrance and the line connection liquid that easily produces electrolysis spills, and pump pond electrolyte inside aggregation corrosive acid pump, cause sour pump short for work-ing life, cost of use is high, uses inconvenience.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of lead electrolytic solution recycle system of easy to use, long service life.
In order to solve the problems of the technologies described above, electrolytic solution reservoir of the present utility model, cyclic acid pump and electrolyzer, also comprise electrolytic solution and retain annular seal space, described electrolytic solution retains annular seal space and to be placed in above electrolytic solution reservoir and electrolytic solution retains annular seal space inner top is provided with into pipe, and this entrance entering pipe is placed in electrolytic solution reservoir electrolytic solution; Described electrolytic solution to retain in annular seal space liquid level higher than cyclic acid pump entrance and electrolytic solution retain bottom annular seal space with cyclic acid pump entrance UNICOM, make electrolytic solution retain in annular seal space and cyclic acid pump internal memory leaves electrolytic solution; Described cyclic acid pump outlet and electrolyzer UNICOM.
It is acid-resistant sealant bucket that described electrolytic solution retains annular seal space.
Acidproof protection pad is provided with below described cyclic acid pump.
Adopt structure of the present utility model, annular seal space is retained owing to also comprising electrolytic solution, electrolytic solution retains annular seal space and to be placed in above electrolytic solution reservoir and electrolytic solution retains annular seal space inner top is provided with into pipe, this entrance entering pipe is placed in electrolytic solution reservoir electrolytic solution, electrolytic solution to retain in annular seal space liquid level higher than cyclic acid pump entrance and electrolytic solution retain bottom annular seal space with cyclic acid pump entrance UNICOM, electrolytic solution is made to retain in annular seal space and cyclic acid pump internal memory leaves electrolytic solution, cyclic acid pump outlet and electrolyzer UNICOM.Electrolytic solution retains in annular seal space and cyclic acid pump internal memory leaves electrolytic solution, without the need at cyclic acid pump portal perfusion electrolytic solution during startup cyclic acid pump, directly turns on the power switch, easy to use, and long service life is simple to operate.
Owing to being provided with acidproof protection pad below cyclic acid pump.Cyclic acid pump is supported on ground by acidproof protection pad, when cyclic acid pump outlet, entrance and line connection electrolytic solution spill and flow in ground, cyclic acid pump shell and bottom can not contact electrolytic solution, prevent electrolytic corrosion cyclic acid pump, cyclic acid pump long service life, use more convenient, operate simpler.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in detail:
As shown in Figure 1, the lead electrolytic solution recycle system of the present utility model, comprises electrolytic solution reservoir 5, cyclic acid pump 1 and electrolyzer 2.Also comprise electrolytic solution and retain acid-resistant sealant bucket 4.Electrolytic solution retains acid-resistant sealant bucket 4 and to be placed in above electrolytic solution reservoir 5 and electrolytic solution retains acid-resistant sealant bucket 4 inner top is provided with into pipe 6, and this entrance entering pipe 6 is placed in electrolytic solution reservoir 5 electrolytic solution.Electrolytic solution to retain in acid-resistant sealant bucket 4 liquid level higher than cyclic acid pump 1 entrance and electrolytic solution retain bottom acid-resistant sealant bucket 4 with cyclic acid pump 1 entrance UNICOM, make electrolytic solution retain in acid-resistant sealant bucket 4 and cyclic acid pump 1 internal memory leaves electrolytic solution.Acid-resistant sealant bucket 4 also can be the annular seal space of other form with identical function.Cyclic acid pump 1 exports and electrolyzer 2 UNICOM.
In order to prevent electrolytic corrosion cyclic acid pump, cyclic acid pump long service life, uses more convenient, operates simpler.Acidproof protection pad 3 is provided with below cyclic acid pump 1.Cyclic acid pump is supported on ground by acidproof protection pad, when cyclic acid pump outlet, entrance and line connection electrolytic solution spill and flow in ground, cyclic acid pump shell and bottom can not contact electrolytic solution, prevent electrolytic corrosion cyclic acid pump, cyclic acid pump long service life, use more convenient, operate simpler.
Claims (3)
1. a lead electrolytic solution recycle system, comprise electrolytic solution reservoir (5), cyclic acid pump (1) and electrolyzer (2), it is characterized in that: also comprise electrolytic solution and retain annular seal space (4), described electrolytic solution retains annular seal space (4) and is placed in electrolytic solution reservoir (5) top and electrolytic solution retains annular seal space (4) inner top is provided with into pipe (6), and this entrance entering pipe (6) is placed in electrolytic solution reservoir (5) electrolytic solution; Described electrolytic solution retains annular seal space (4) interior liquid level higher than cyclic acid pump (1) entrance and electrolytic solution retains annular seal space (4) bottom and cyclic acid pump (1) entrance UNICOM, makes electrolytic solution retain in annular seal space (4) and cyclic acid pump (1) internal memory leaves electrolytic solution; Described cyclic acid pump (1) outlet and electrolyzer (2) UNICOM.
2. the lead electrolytic solution recycle system according to claim 1, is characterized in that: it is acid-resistant sealant bucket that described electrolytic solution retains annular seal space (4).
3. the lead electrolytic solution recycle system according to claim 1, is characterized in that: described cyclic acid pump (1) below is provided with acidproof protection pad (3).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420492152.3U CN204162803U (en) | 2014-08-29 | 2014-08-29 | The lead electrolytic solution recycle system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420492152.3U CN204162803U (en) | 2014-08-29 | 2014-08-29 | The lead electrolytic solution recycle system |
Publications (1)
Publication Number | Publication Date |
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CN204162803U true CN204162803U (en) | 2015-02-18 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201420492152.3U Expired - Fee Related CN204162803U (en) | 2014-08-29 | 2014-08-29 | The lead electrolytic solution recycle system |
Country Status (1)
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CN (1) | CN204162803U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107268029A (en) * | 2017-06-30 | 2017-10-20 | 湘潭大学 | The method and apparatus that a kind of waterpower unloads the lead solution continuous electrolysis of lead |
-
2014
- 2014-08-29 CN CN201420492152.3U patent/CN204162803U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107268029A (en) * | 2017-06-30 | 2017-10-20 | 湘潭大学 | The method and apparatus that a kind of waterpower unloads the lead solution continuous electrolysis of lead |
CN107268029B (en) * | 2017-06-30 | 2019-08-06 | 湘潭大学 | The method and apparatus that a kind of waterpower unloads the lead solution continuous electrolysis of lead |
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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 | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150218 Termination date: 20170829 |