CN103103559A - Ionic membrane electrolytic bath - Google Patents
Ionic membrane electrolytic bath Download PDFInfo
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- CN103103559A CN103103559A CN2012105385336A CN201210538533A CN103103559A CN 103103559 A CN103103559 A CN 103103559A CN 2012105385336 A CN2012105385336 A CN 2012105385336A CN 201210538533 A CN201210538533 A CN 201210538533A CN 103103559 A CN103103559 A CN 103103559A
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- electrode
- ionic membrane
- electrolyzer
- electrolytic bath
- ion
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Abstract
The invention relates to an ionic membrane electrolytic bath which comprises an electrolytic bath body, a bath cover matched with the electrolytic bath, a cathode net, an anode net and an ionic membrane. The electrolytic bath is provided with an electrolyte inlet and an electrolyte outlet, the bath cover of the electrolytic bath is provided with air outlets, the cathode net and the anode net are arranged in the electrolytic bath relatively in parallel, the ionic membrane is arranged between the cathode net and the anode net, and separates the electrolytic bath into two parts, particle electrodes are respectively filled between the cathode net and the ionic membrane as well as between the anode net and the ionic membrane. A cathode plate, an anode plate and the particle electrodes form a multidimensional electrode reaction system, wherein a catalytic material coating is loaded on the particle electrodes which are filled between the anode and cathode plates, and the electrolytic efficiency is greatly improved.
Description
Technical field
The present invention relates to a kind of ion-exchange membrane electrolyzer, be specifically related to a kind of ion-exchange membrane electrolyzer that is filled with granule electrode.
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.
Traditional electrolytic cell equipment is simple two-dimensional flat plate electric pole type, 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 that Area Ratio is little, the space-time treatment capacity is few, current efficiency is low, energy consumption is large, the high cost shortcoming, and production efficiency is not high.
Multidimension electrode is the granule electrode of filling the granulated material formation between two-dimensional electrode passing, and the Area Ratio that the three-diemsnional electrode electrocatalysis is processed increases greatly, and spacing of particle is little, thereby mass transfer in liquid phase efficient is high.But existing three-dimensional catalytic treatment equipment is slower for the electrolytic solution speed of processing high density.
Summary of the invention
The technical problem to be solved in the present invention is: propose a kind of ion-exchange membrane electrolyzer high to the high salt concentration water treatment efficiency.
The present invention is that the technical scheme that solves the problems of the technologies described above proposition is: a kind of ion-exchange membrane electrolyzer, the groove lid, cathode screen, anode network and the ionic membrane that comprise electrolytic cell body, match with described electrolyzer, described cell body is provided with the electrolytic solution import and export, described electrolytic bath covers and is provided with the air outlet, being located in electrolyzer of described cathode screen and anode network opposing parallel, described ionic membrane is located between the yin, yang polar net and with described electrolyzer and is divided into two portions, all is filled with granule electrode between described cathode screen and ionic membrane, anode network and ionic membrane.
The invention has the beneficial effects as follows:
Yin, yang pole plate of the present invention and the granule electrode that is filled between pole plate have consisted of the multidimension electrode reactive system jointly, have greatly improved electrolytic efficiency.
Having improved of technique scheme:
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 that forms.
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 present invention 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.
Description of drawings
Below in conjunction with accompanying drawing, the ion-exchange membrane electrolyzer that is filled with granule electrode in the present invention is described further.
Fig. 1 is the structural representation of embodiment intermediate ion membrane electrolyser.
Embodiment
Embodiment
According to shown in Figure 1, the ion-exchange membrane electrolyzer in the present invention, the groove lid 2, cathode screen 3, anode network 4 and the ionic membrane 5 that comprise electrolytic cell body 1, match with electrolyzer.
Wherein, cell body 1 is provided with electrolytic solution import and export 6,7, and electrolytic bath lid 2 is provided with air outlet 8.
Wherein, being located in electrolyzer of cathode screen 3 and anode network 4 opposing parallel, ionic membrane 5 is located between yin, yang polar net 3,4 and with electrolyzer and is divided into two portions, all is filled with granule electrode 9 between cathode screen 3 and ionic membrane 5, anode network 4 and ionic membrane 5.
The above-described embodiment that is not limited to of the present invention, all employings are equal to replaces the technical scheme that forms, and all drops in the protection domain of requirement of the present invention.
Claims (4)
1. ion-exchange membrane electrolyzer, the groove lid, cathode screen, anode network and the ionic membrane that comprise electrolytic cell body, match with described electrolyzer, described cell body is provided with the electrolytic solution import and export, described electrolytic bath covers and is provided with the air outlet, being located in electrolyzer of described cathode screen and anode network opposing parallel, described ionic membrane is located between the yin, yang polar net and with described electrolyzer and is divided into two portions, it is characterized in that: all be filled with granule electrode between described cathode screen and ionic membrane, anode network and ionic membrane.
2. ion-exchange membrane electrolyzer according to claim 1 is characterized in that: described 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 that forms.
3. ion-exchange membrane electrolyzer according to claim 2, 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. ion-exchange membrane electrolyzer according to claim 2 is characterized in that: 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.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012105385336A CN103103559A (en) | 2012-12-13 | 2012-12-13 | Ionic membrane electrolytic bath |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012105385336A CN103103559A (en) | 2012-12-13 | 2012-12-13 | Ionic membrane electrolytic bath |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103103559A true CN103103559A (en) | 2013-05-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012105385336A Pending CN103103559A (en) | 2012-12-13 | 2012-12-13 | Ionic membrane electrolytic bath |
Country Status (1)
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| CN (1) | CN103103559A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105780047A (en) * | 2014-12-25 | 2016-07-20 | 佛山市宝航机械装备行业知识产权服务有限公司 | Efficient safe electrolytic bath |
| WO2016141768A1 (en) * | 2015-03-09 | 2016-09-15 | 罗民雄 | Electrode mainly prepared from ceramic material and applicable to water electrolysis device |
| CN109750315A (en) * | 2017-11-07 | 2019-05-14 | 丹阳市日晟工业设备有限公司 | High-effect ionic membrane electrolysis cells |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2459329Y (en) * | 2000-12-14 | 2001-11-14 | 深圳市柯雷恩环境科技有限公司 | Anion membrane electrolytic bath |
| CN201325897Y (en) * | 2008-11-18 | 2009-10-14 | 南京赛佳环保科技有限责任公司 | Waste water treatment equipment of multi-dimensional electrode electrical catalytic reactor of horizontal electrode plate |
| CN203065587U (en) * | 2012-12-13 | 2013-07-17 | 苏州新区化工节能设备厂 | Ion-exchange membrane electrolytic bath |
-
2012
- 2012-12-13 CN CN2012105385336A patent/CN103103559A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2459329Y (en) * | 2000-12-14 | 2001-11-14 | 深圳市柯雷恩环境科技有限公司 | Anion membrane electrolytic bath |
| CN201325897Y (en) * | 2008-11-18 | 2009-10-14 | 南京赛佳环保科技有限责任公司 | Waste water treatment equipment of multi-dimensional electrode electrical catalytic reactor of horizontal electrode plate |
| CN203065587U (en) * | 2012-12-13 | 2013-07-17 | 苏州新区化工节能设备厂 | Ion-exchange membrane electrolytic bath |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105780047A (en) * | 2014-12-25 | 2016-07-20 | 佛山市宝航机械装备行业知识产权服务有限公司 | Efficient safe electrolytic bath |
| WO2016141768A1 (en) * | 2015-03-09 | 2016-09-15 | 罗民雄 | Electrode mainly prepared from ceramic material and applicable to water electrolysis device |
| CN109750315A (en) * | 2017-11-07 | 2019-05-14 | 丹阳市日晟工业设备有限公司 | High-effect ionic membrane electrolysis cells |
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Application publication date: 20130515 |