CN202786449U - Electrolysis electrode structure - Google Patents
Electrolysis electrode structure Download PDFInfo
- Publication number
- CN202786449U CN202786449U CN 201220364589 CN201220364589U CN202786449U CN 202786449 U CN202786449 U CN 202786449U CN 201220364589 CN201220364589 CN 201220364589 CN 201220364589 U CN201220364589 U CN 201220364589U CN 202786449 U CN202786449 U CN 202786449U
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- China
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- electrode
- axostylus axostyle
- electrolysis
- electrode structure
- support shaft
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Abstract
The utility model discloses an electrolysis electrode structure. The electrode comprises a positive electrode and a negative electrode, wherein the positive electrode is connected with a positive terminal; the negative electrode is connected with a negative terminal; the positive electrode is a wire-braided support shaft lever; the negative electrode is an outer circular sleeve net; the outer circular sleeve net is sleeved outside the support shaft lever; and the support shaft lever is provided with a spiral guiding and blocking rack, thereby forming a spiral section channel in a clearance between the outer circular sleeve net and the support shaft lever. According to electrolysis electrode structure, the wire-braided support shaft lever and the outer circular sleeve net are used, and the spiral guiding and blocking rack is arranged in the clearance between the outer circular sleeve net and the support shaft lever so as to form the spiral section channel, so that the effective contact time of sewage and the electrode can be prolonged, thereby improving the electrolysis effect without increasing the cost.
Description
Technical field
The utility model relates to a kind of electrolyzer, is specifically related to a kind of electrolysis electrode structure.
Background technology
Electrolyzer be by anodal, negative electrode by solution as conductor, under the effect of electric current and voltage, produce the electrochemical reaction redox that the move toward one another of electronics produces, shown in Fig. 1.Dissolved substance when redox continues to occur in the electrolytic solution is separated by coacervation with suspended substance, thereby reaches the purpose of repaying principal and radically reforming.
If sewage is reached this purpose of radically reforming of repaying principal through electrolysis, at first must satisfy following 5 primary conditions: 1) load voltage is determined; 2) current density is determined; 3) time of electrolytic action; 4) electrode specific surface area is determined; 5) effluent flow rate is determined.After voltage and current density was determined, the time of electrolytic action and electrode specific surface area were determining the effect of electrolysis, and whether the electrolytic action time effectively contacts with electrode with electrolytic solution and related.
Existing electrolytic solution treatment process battery lead plate form has plate type electrode (plane) or ring-shaped electrode.Plate type electrode is if when reaching desirable treatment effect, power consumption is high, and the treatment time is long, the running cost height, and facility investment is large; Though ring type electrode is better than plate type electrode at treatment effect, but because sewage and electrode are short effective duration of contact, do not reach the timeliness requirement, require then to need to prolong electrode length as reaching timeliness, when ring electrode reaches certain-length, manufacturing has brought difficulty to electrode, has also strengthened the manufacturing cost of electrolyzer simultaneously.Electrode area increases its power consumption and increases, and running cost increases.
Therefore, obtain prolonging effective duration of contact in order to make electrolytic solution and electrode, be necessary existing plane formula electrode and ring type electrode are improved.
The utility model content
The purpose of this utility model is to overcome the defective that exists in the prior art, provides a kind of electrolytic solution to process electrolysis electrode, prolongs electrolytic solution and electrode effective duration of contact, improves electrolysis effectiveness and does not increase cost.
For achieving the above object, the technical solution of the utility model is a kind of electrolysis electrode structure of design, described electrode comprises positive electrode and negative potential, described positive electrode is connected with positive terminal, described negative potential is connected with negative terminal, it is characterized in that, described positive electrode is the support axostylus axostyle by metal wire knitted, described negative electricity is cylindrical cover net very, described cylindrical cover net is outside supporting axostylus axostyle, described support axostylus axostyle is provided with spiral diversion and intercepts tooth bar, thereby forms spiral segment groove passage in the gap between cylindrical cover net and support axostylus axostyle.
Wherein preferred technical scheme is, described support axostylus axostyle is the metal cylinder rod by two kinds of metal wire knitted of titanium nickel, and described cylindrical cover net is cylindrical titanium nickel wire netting.
Preferred technical scheme also has, and described spiral diversion intercepts tooth bar and is the insulation tooth bar.
Preferred technical scheme also has, and described titanium nickel diameter wiry is 0.05mm ~ 0.1mm.
Advantage of the present utility model and beneficial effect are: this electrolysis electrode structure, the support axostylus axostyle of employing technology silk braiding and cylindrical cover net, and the place, crack is provided with spiral diversion obstruct tooth bar formation spiral segment groove passage betwixt, thereby prolong sewage and electrode effective duration of contact, improve electrolysis effectiveness and do not increase cost.
Description of drawings
Fig. 1 is the utility model electrolysis principle figure;
Fig. 2 is the synoptic diagram of the utility model electrolysis electrode structure.
Embodiment
Below in conjunction with drawings and Examples, embodiment of the present utility model is further described.Following examples only are used for the technical solution of the utility model more clearly is described, and can not limit protection domain of the present utility model with this.
As shown in Figure 1, 2, the utility model is that a kind of electrolytic solution is processed electrolysis electrode, prolongs electrolytic solution and electrode effective duration of contact, improves electrolysis effectiveness and does not increase cost.
For achieving the above object, the technical solution of the utility model is a kind of electrolysis electrode structure of design, described electrode comprises positive electrode and negative potential, described positive electrode is connected with positive terminal 5, described negative potential is connected with negative terminal 4, this positive electrode is the support axostylus axostyle 1 by metal wire knitted, described negative electricity is cylindrical cover net 3 very, described cylindrical cover net 3 is outside supporting axostylus axostyle 1, described support axostylus axostyle 1 is provided with spiral diversion and intercepts tooth bar 2, thereby forms spiral segment groove passage 6 in the gap between cylindrical cover net 3 and support axostylus axostyle.
Preferred embodiment is in the utility model, and described support axostylus axostyle is the metal cylinder rod by two kinds of metal wire knitted of titanium nickel, and described cylindrical cover net is cylindrical titanium nickel wire netting.
Preferred embodiment also has in the utility model, and described spiral diversion intercepts tooth bar 3 and is the insulation tooth bar.
Preferred embodiment also has in the utility model, and described titanium nickel diameter wiry is 0.05mm ~ 0.1mm.
The above only is preferred implementation of the present utility model; should be understood that; for those skilled in the art; under the prerequisite that does not break away from the utility model know-why; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (4)
1. electrolysis electrode structure, described electrode comprises positive electrode and negative potential, described positive electrode is connected with positive terminal (5), described negative potential is connected with negative terminal (4), it is characterized in that, described positive electrode is the support axostylus axostyle (1) by metal wire knitted, described negative electricity is cylindrical cover net (3) very, described cylindrical cover net (3) is enclosed within and supports outside the axostylus axostyle (1), described support axostylus axostyle (1) is provided with spiral diversion and intercepts tooth bar (2), thereby forms spiral segment groove passage (6) in the gap between cylindrical cover net (3) and support axostylus axostyle (1).
2. electrolysis electrode structure as claimed in claim 1 is characterized in that, described support axostylus axostyle (1) is that described cylindrical cover net (3) is cylindrical titanium nickel wire netting by the metal cylinder rod of two kinds of metal wire knitted of titanium nickel.
3. electrolysis electrode structure as claimed in claim 1 is characterized in that, described spiral diversion intercepts tooth bar (2) and is the insulation tooth bar.
4. electrolysis electrode structure as claimed in claim 2 is characterized in that, described titanium nickel diameter wiry is 0.05mm ~ 0.1mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220364589 CN202786449U (en) | 2012-07-25 | 2012-07-25 | Electrolysis electrode structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220364589 CN202786449U (en) | 2012-07-25 | 2012-07-25 | Electrolysis electrode structure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202786449U true CN202786449U (en) | 2013-03-13 |
Family
ID=47813746
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220364589 Expired - Lifetime CN202786449U (en) | 2012-07-25 | 2012-07-25 | Electrolysis electrode structure |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202786449U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109097795A (en) * | 2018-08-27 | 2018-12-28 | 深圳市世清环保科技有限公司 | A kind of wound form cathode assembly |
-
2012
- 2012-07-25 CN CN 201220364589 patent/CN202786449U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109097795A (en) * | 2018-08-27 | 2018-12-28 | 深圳市世清环保科技有限公司 | A kind of wound form cathode assembly |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP03 | Change of name, title or address |
Address after: 214400 Wuxi City, Jiangyin Province town industrial park on the East Road, No. 221 on Patentee after: JIANGSU ANCAN TECHNOLOGY CO.,LTD. Address before: 214400, No. 221 East Road, Town Industrial Park, Jiangyin, Wuxi, Jiangsu, Jiangsu Patentee before: Jiangyin Ancan Electrochemical Equipment Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130313 |