CN203065589U - Single-anode two-cathode ionic membrane electrolytic unit bath - Google Patents
Single-anode two-cathode ionic membrane electrolytic unit bath Download PDFInfo
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- CN203065589U CN203065589U CN201220688008.8U CN201220688008U CN203065589U CN 203065589 U CN203065589 U CN 203065589U CN 201220688008 U CN201220688008 U CN 201220688008U CN 203065589 U CN203065589 U CN 203065589U
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Abstract
The utility model relates to a single-anode two-cathode ionic membrane electrolytic unit bath, comprising a bath body, a cover body matched with the bath body, cathode and anode nets arranged in the bath body, and an ionic membrane arranged between the cathode net and the anode net to separate the cathode nets from the anode net, wherein an electrolyte inlet and an electrolyte outlet are arranged in the bath body; a gas outlet is formed in the cover body; the number of the cathode nets is two, and one anode net which is arranged between the two cathode nets; and the cathode nets and the anode net are arranged in the bath body vertically and in parallel with each other. The single-anode two-cathode ionic membrane electrolytic unit bath is characterized in that two cathode nets are arranged in one previous unit bath and enabled to share one anode net skillfully so that the utilization efficiency of the anode net is improved and the production efficiency of the unit bath is effectively improved.
Description
Technical field
The utility model relates to a kind of ion-exchange membrane electrolyzer, is specifically related to a kind of single anode double cathode ion-exchange membrane electrolyzer.
Background technology
Ion-exchange membrane electrolyzer be at present in chlorine industry for the production of the equipment of the main use of alkali lye, hydrogen and chlorine.Ion-exchange membrane electrolyzer is to be made of a plurality of unit grooves with yin, yang polar net and ionic membrane.
Traditional electrolytic cell equipment is simple two-dimensional plate electrode formula, equipment body is made of vertical placement, opposing parallel, interlaced yin, yang pole plate, auxiliary with power supply, the yin, yang pole plate can be the metal sheet of unlike material, the equipment of ion-exchange membrane electrolyzer exists area than little, shortcomings such as the space-time treatment capacity is lacked, current efficiency is low, energy consumption is big, cost height, and production efficiency is not high.
Therefore, develop a kind of cost savings, the electrolyzer that efficient improves becomes the problem of needing solution badly.
The utility model content
The technical problems to be solved in the utility model is: propose a kind ofly can not enlarge unit groove cell body size and improve the electrolysis unit groove of electrolytic efficiency.
The utility model is that the technical scheme that solves the problems of the technologies described above proposition is: a kind of single anode double cathode ion membrane electrolysis unit tank, comprise cell body, the lid that matches with described cell body, be located at the moon in the described cell body, anode network and be located at described the moon, between the anode network and with described the moon, the ionic membrane that anode network is separated by, described cell body is provided with electrolytic solution and advances, outlet, described lid is provided with the air outlet, described cathode screen is two, described anode network is one and is located between described two cathode screens described the moon, the anode network three vertically and being located in the described cell body of being parallel to each other.
The beneficial effects of the utility model are:
The utility model is by arranging the jack to jack adapter polar net in an original unit groove, and makes its shared a slice anode network cleverly, thereby strengthened the service efficiency of anode network, effectively promoted the production efficiency of unit groove.
Having improved of technique scheme:
In order to have constituted the multidimension electrode reactive system, be filled with granule electrode between the described yin, yang polar net.
Further improving of granule electrode had: by load by the ceramic particle of catalytic specie coating, uncoated ceramic particle and gac by volume 2:2:1 evenly mix the Bipolar Micro-Electrode electrode of forming.
More abundant for electrolysis, the Bipolar Micro-Electrode electrode of filling between negative plate, positive plate has vesicular structure, and the particle diameter of Bipolar Micro-Electrode electrode is the 3-5 millimeter.
To further improving of technical scheme in the utility model be: it is complex metal oxides tindioxide, antimonous oxide and Manganse Dioxide that load has the catalytic specie of the ceramic particle institute load of catalytic specie coating.
Further application to unit groove in the utility model is: have at least two described unit grooves to carry out the parallel connection combination.
Description of drawings
Below in conjunction with accompanying drawing single anode double cathode ion membrane electrolysis unit tank of the present utility model is described further.
Fig. 1 is the structural representation of single anode double cathode ion membrane electrolysis unit tank in the utility model.
Embodiment
Embodiment
Shown in Fig. 1, single anode double cathode ion membrane electrolysis unit tank in the utility model comprises cell body 1, and the lid 2 that matches of cell body 1, is located at yin, yang polar net 3 in the cell body 1,4 and be located at the ionic membrane 5 of between the yin, yang polar net 3,4 yin, yang polar net 3,4 being separated by.
Wherein, cell body is provided with electrolytic solution and advances 2, exports 6, and lid is provided with air outlet 7.
Wherein, cathode screen 3 is two, and anode network 4 is one and is located between two cathode screens 3, and yin, yang polar net 3,4 threes are vertically and being located in the cell body 1 of being parallel to each other.
Between yin, yang polar net 3,4, be filled with the granule electrode (not shown).Granule electrode by load by the ceramic particle of catalytic specie coating, uncoated ceramic particle and gac by volume 2:2:1 evenly mix the Bipolar Micro-Electrode electrode of forming.The Bipolar Micro-Electrode electrode of filling between negative plate, positive plate has vesicular structure, and the particle diameter of Bipolar Micro-Electrode electrode is the 3-5 millimeter.It is complex metal oxides tindioxide, antimonous oxide and Manganse Dioxide that load has the catalytic specie of the ceramic particle institute load of catalytic specie coating.
For more high efficiency production, a plurality of unit grooves can be carried out the parallel connection combination.
The above-described embodiment that is not limited to of the present utility model, all employings are equal to replaces the technical scheme that forms, and all drops in the protection domain of the utility model requirement.
Claims (4)
1. single anode double cathode ion membrane electrolysis unit tank, comprise cell body, and the lid that matches of described cell body, the ionic membrane that is located at the yin, yang polar net in the described cell body and is located between the described yin, yang polar net and described yin, yang polar net is separated by, described cell body is provided with the electrolytic solution import and export, described lid is provided with the air outlet, it is characterized in that: described cathode screen is two, described anode network is one and is located between described two cathode screens, and described yin, yang polar net three vertically and being located in the described cell body of being parallel to each other.
2. according to the described single anode double cathode ion membrane electrolysis unit tank of claim 1, it is characterized in that: be filled with granule electrode between the described yin, yang polar net.
3. according to the described single anode double cathode ion membrane electrolysis unit tank of claim 1, it is characterized in that: the Bipolar Micro-Electrode electrode of filling between negative plate, positive plate has vesicular structure, and the particle diameter of Bipolar Micro-Electrode electrode is the 3-5 millimeter.
4. according to the described single anode double cathode ion membrane electrolysis unit tank of claim 1, it is characterized in that: at least two described unit grooves carry out the parallel connection combination.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220688008.8U CN203065589U (en) | 2012-12-13 | 2012-12-13 | Single-anode two-cathode ionic membrane electrolytic unit bath |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220688008.8U CN203065589U (en) | 2012-12-13 | 2012-12-13 | Single-anode two-cathode ionic membrane electrolytic unit bath |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203065589U true CN203065589U (en) | 2013-07-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201220688008.8U Expired - Fee Related CN203065589U (en) | 2012-12-13 | 2012-12-13 | Single-anode two-cathode ionic membrane electrolytic unit bath |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203065589U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103114300A (en) * | 2012-12-13 | 2013-05-22 | 苏州新区化工节能设备厂 | Single-anode double-cathode ion-exchange membrane electrolytic unit cell |
| CN103526225A (en) * | 2013-10-10 | 2014-01-22 | 武汉远大弘元股份有限公司 | Double-layer meshy negative electrode electrolytic bath |
| CN103726067A (en) * | 2013-12-24 | 2014-04-16 | 柳州豪祥特科技有限公司 | Electrolysis system for producing electrolytic manganese dioxide |
| CN104005045A (en) * | 2014-06-11 | 2014-08-27 | 北京首位能源科技有限公司 | Extendable combined multi-polar electrolytic bath |
-
2012
- 2012-12-13 CN CN201220688008.8U patent/CN203065589U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103114300A (en) * | 2012-12-13 | 2013-05-22 | 苏州新区化工节能设备厂 | Single-anode double-cathode ion-exchange membrane electrolytic unit cell |
| CN103526225A (en) * | 2013-10-10 | 2014-01-22 | 武汉远大弘元股份有限公司 | Double-layer meshy negative electrode electrolytic bath |
| CN103526225B (en) * | 2013-10-10 | 2017-01-18 | 武汉远大弘元股份有限公司 | Double-layer meshy negative electrode electrolytic bath |
| CN103726067A (en) * | 2013-12-24 | 2014-04-16 | 柳州豪祥特科技有限公司 | Electrolysis system for producing electrolytic manganese dioxide |
| CN103726067B (en) * | 2013-12-24 | 2016-08-24 | 柳州豪祥特科技有限公司 | A kind of electrolysis system producing electrolytic manganese dioxide |
| CN104005045A (en) * | 2014-06-11 | 2014-08-27 | 北京首位能源科技有限公司 | Extendable combined multi-polar electrolytic bath |
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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: 20130717 Termination date: 20131213 |