CN203247315U - Bipolar electrolysis bath - Google Patents
Bipolar electrolysis bath Download PDFInfo
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- CN203247315U CN203247315U CN 201320200883 CN201320200883U CN203247315U CN 203247315 U CN203247315 U CN 203247315U CN 201320200883 CN201320200883 CN 201320200883 CN 201320200883 U CN201320200883 U CN 201320200883U CN 203247315 U CN203247315 U CN 203247315U
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- bipolar
- electrolyzer
- electrolysis
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Abstract
The utility model discloses a bipolar electrolysis bath, which comprises at least one electrolysis bath, wherein the electrodes of all electrolysis baths are bipolar electrodes. According to the bipolar electrolysis bath, the individual electrolysis bath of the bipolar electrode structure can be connected in series to be a plurality of electrolysis chambers, that is, one bipolar electrolysis bath is equivalent to the integration of the plurality of homopolar electrolysis baths; as the working current of the series connection is smaller, the current distribution on the electrode surface is uniform, the structure of the electrolysis baths is compact, and the maintenance is convenient.
Description
Technical field
The utility model relates to a kind of lost currents.
Background technology
At present, the Electrowinning clorox is used widely, because early stage electrolyzer adopts the unipolarity electrode to limit the development of large-scale chlorine equipment processed, as shown in Figure 1, this structure has very large shortcoming, and for example: working current is larger, and the electrode surface distribution of current is inhomogeneous; Extremely complicated copper bar is connected with bolt and the contact resistance that causes is large, and electric energy loss is large; Trim is large, the many and inevitable leakage problems that produces of trim.
The utility model content
Technical problem to be solved in the utility model is the shortcoming that overcomes the electrolyzer of existing unipolarity electrode, for this reason, provides a kind of lost currents.
It is as follows that the utility model solves the problems of the technologies described above the technical scheme of taking: a kind of lost currents, comprise one or more electrolyzer, and wherein, the electrode structure of each electrolyzer is bipolar electrode.
Further, the electrode structure of described one or more electrolyzer is connected each other.
Further, described one or more electrolyzer adopts the plain-straight-face flange sealing to connect with O type circle sealing member each other.
The beneficial effects of the utility model are as follows: the single electrolyzer of bipolar electrode configurations can be connected into more tank room, namely a bipolar system electrolyzer is equivalent to the integrated of a plurality of monopolar electrolyzers, because it is less to be connected in series working current, the electrode surface distribution of current is even, cell construction is compact, and is easy to maintenance.
Other features and advantages of the utility model will be set forth in the following description, and, partly from specification sheets, become apparent, perhaps understand by implementing the utility model.The purpose of this utility model and other advantages can realize and obtain by specifically noted structure in the specification sheets of writing, claims and accompanying drawing.
Description of drawings
Below in conjunction with accompanying drawing the utility model is described in detail, makes above-mentioned advantage of the present utility model clearer and more definite.
Fig. 1 is the structural representation of prior art.
Fig. 2 is the structural representation of lost currents of the present invention.
Fig. 3 is the partial approach synoptic diagram of lost currents of the present invention.
Embodiment
Below in conjunction with specific embodiment the utility model is described in detail.
As shown in Figures 2 and 3, lost currents of the present utility model comprises one or more electrolyzer, and wherein, the electrode structure of each electrolyzer is bipolar electrode.
The electrode structure of described one or more electrolyzer is connected each other.
Described one or more electrolyzer adopts the plain-straight-face flange sealing to connect with O type circle sealing member each other.
Wherein, the electrode structure of electrolyzer is bipolar electrode (being compound electrode), with respect to the unipolarity electrode structure, bipolar electrode has the following advantages: 1) the single electrolyzer of bipolar electrode configurations can be connected into more tank room, namely a bipolar system electrolyzer is equivalent to the integrated of a plurality of monopolar electrolyzers, because it is less to be connected in series working current, the electrode surface distribution of current is even, cell construction is compact, and is easy to maintenance; 2) the electrical ties mode of bipolar electrode configurations adopts electrode to be connected salt solution/seawater with ionogen) conduction connects, the even distribution of electric current and less ohm voltage drop have been guaranteed, higher current efficiency, the copper bar of having avoided unipolarity electrode complexity is connected with bolt and the contact resistance that causes is large, and electric energy loss is large; 3) the connection number of times is few between lost currents, and trim is little, adopts simultaneously plain-straight-face flange sealing and O type circle sealing member, has guaranteed complete assembly long-time running ne-leakage.It is large to have overcome unipolarity electrode trim, the many and inevitable leakage problems that produces of trim.
The above only is preferred embodiment of the present utility model, be not limited to the utility model, although with reference to previous embodiment the utility model is had been described in detail, for a person skilled in the art, it still can be made amendment to the technical scheme that aforementioned each embodiment puts down in writing, and perhaps part technical characterictic wherein is equal to replacement.All within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., all should be included within the protection domain of the present utility model.
Claims (3)
1. a lost currents is characterized in that, comprises one or more electrolyzer, and wherein, the electrode structure of each electrolyzer is bipolar electrode.
2. lost currents according to claim 1 is characterized in that, the electrode structure of described one or more electrolyzer is connected each other.
3. lost currents according to claim 1 and 2 is characterized in that, described one or more electrolyzer adopts the plain-straight-face flange sealing to connect with O type circle sealing member each other.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320200883 CN203247315U (en) | 2013-04-21 | 2013-04-21 | Bipolar electrolysis bath |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320200883 CN203247315U (en) | 2013-04-21 | 2013-04-21 | Bipolar electrolysis bath |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203247315U true CN203247315U (en) | 2013-10-23 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320200883 Expired - Lifetime CN203247315U (en) | 2013-04-21 | 2013-04-21 | Bipolar electrolysis bath |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203247315U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103969305A (en) * | 2014-04-30 | 2014-08-06 | 陕西师范大学 | Bipolar-electrode electrochemiluminescence imaging electrolytic cell |
| CN107119284A (en) * | 2017-06-27 | 2017-09-01 | 中国灌溉排水发展中心 | A kind of batch (-type) electrolyzes table salt hypochlorite generator |
| CN109208035A (en) * | 2018-10-23 | 2019-01-15 | 攀钢集团攀枝花钢铁研究院有限公司 | Electrolysis production system and its construction method for magnesiothermy production titanium sponge |
| CN111156753A (en) * | 2018-11-07 | 2020-05-15 | 博西华电器（江苏）有限公司 | Gas conditioning system and refrigeration appliance |
| CN111156727A (en) * | 2018-11-07 | 2020-05-15 | 博西华电器（江苏）有限公司 | Oxygen reduction device, gas regulating system and refrigeration appliance |
| CN111156728A (en) * | 2018-11-07 | 2020-05-15 | 博西华电器（江苏）有限公司 | Oxygen reduction device, gas regulating system and refrigeration appliance |
-
2013
- 2013-04-21 CN CN 201320200883 patent/CN203247315U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103969305A (en) * | 2014-04-30 | 2014-08-06 | 陕西师范大学 | Bipolar-electrode electrochemiluminescence imaging electrolytic cell |
| CN107119284A (en) * | 2017-06-27 | 2017-09-01 | 中国灌溉排水发展中心 | A kind of batch (-type) electrolyzes table salt hypochlorite generator |
| CN109208035A (en) * | 2018-10-23 | 2019-01-15 | 攀钢集团攀枝花钢铁研究院有限公司 | Electrolysis production system and its construction method for magnesiothermy production titanium sponge |
| CN111156753A (en) * | 2018-11-07 | 2020-05-15 | 博西华电器（江苏）有限公司 | Gas conditioning system and refrigeration appliance |
| CN111156727A (en) * | 2018-11-07 | 2020-05-15 | 博西华电器（江苏）有限公司 | Oxygen reduction device, gas regulating system and refrigeration appliance |
| CN111156728A (en) * | 2018-11-07 | 2020-05-15 | 博西华电器（江苏）有限公司 | Oxygen reduction device, gas regulating system and refrigeration appliance |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20131023 |
|
| CX01 | Expiry of patent term |