Ozone electrolysis structure and electrolysis chamber

文档序号:1486305 发布日期:2020-02-28 浏览:32次 中文

阅读说明:本技术 一种臭氧电解结构及电解室 (Ozone electrolysis structure and electrolysis chamber ) 是由 潘裕富 钟建华 张文英 于 2019-10-16 设计创作,主要内容包括:一种臭氧电解结构,包括间隔设置的阳极片和阴极片,所述阳极片位于进水端,所述阴极片位于出水端,所述阳极片和阴极片之间设有主质子交换膜;所述阳极片上设有进水孔,所述主质子交换膜上设有通水孔,所述阴极片在进水侧的侧面上设有凸起结构。本发明用于制备臭氧水时,能够避免电极表面堆积水垢,提高电极的使用寿命,同时提高臭氧制备效率降低电解能耗,具有臭氧水浓度高,耗能低以及使用寿命长的优点。(An ozone electrolysis structure comprises an anode sheet and a cathode sheet which are arranged at intervals, wherein the anode sheet is positioned at a water inlet end, the cathode sheet is positioned at a water outlet end, and a main proton exchange membrane is arranged between the anode sheet and the cathode sheet; the anode sheet is provided with a water inlet, the main proton exchange membrane is provided with a water through hole, and the cathode sheet is provided with a convex structure on the side surface of the water inlet side. When the method is used for preparing ozone water, scale accumulation on the surface of the electrode can be avoided, the service life of the electrode is prolonged, the ozone preparation efficiency is improved, the electrolysis energy consumption is reduced, and the method has the advantages of high ozone water concentration, low energy consumption and long service life.)

1. An ozone electrolysis structure, characterized in that: the device comprises an anode sheet and a cathode sheet which are arranged at intervals, wherein the anode sheet is positioned at a water inlet end, the cathode sheet is positioned at a water outlet end, and a main proton exchange membrane is arranged between the anode sheet and the cathode sheet; the anode sheet is provided with a water inlet, the main proton exchange membrane is provided with a water through hole, and the cathode sheet is provided with a convex structure or a concave structure on the side surface of the water inlet side.

2. The ozone electrolysis structure according to claim 1, wherein: the side surface of the main proton exchange membrane on the water inlet side is provided with a convex structure or a concave structure.

3. The ozone electrolysis structure according to claim 1 or 2, wherein: the protruding structure comprises at least one of a rectangular protrusion, a circular protrusion, a trapezoidal protrusion, an oval protrusion, a triangular protrusion, an arrow-shaped protrusion, a star-shaped protrusion and an irregular protrusion.

4. The ozone electrolysis structure according to claim 3, wherein: protruding structure is arrow shape arch, and arrow shape arch sets up along the radial direction of limbers, and arrow shape bellied arrow head is outwards.

5. The ozone electrolysis structure according to claim 4, wherein: the number of the protruding structures is a plurality, and the protruding structures are distributed equally along the same circumference by taking the hole center of the limber hole as the circle center.

6. The ozone electrolysis structure according to claim 1 or 2, wherein: the recessed structure includes at least one of a rectangular recess, a circular recess, a trapezoidal recess, an oval recess, a triangular recess, an arrow-shaped recess, a star-shaped recess, and an irregularly-shaped recess.

7. The ozone electrolysis structure according to claim 6, wherein: the recessed structure is arrow-shaped sunken, and arrow-shaped sunken along the radial direction setting of limbers, arrow-shaped sunken arrow outwards.

8. The ozone electrolysis structure according to claim 7, wherein: the number of the concave structures is a plurality, and the concave structures are distributed uniformly along the same circumference by taking the hole center of the limber hole as the circle center.

9. The ozone electrolysis structure according to claim 1, wherein: the ratio of the distance between the anode sheet and the main proton exchange membrane to the distance between the cathode sheet and the main proton exchange membrane is 1: 3.

10. The ozone electrolysis structure according to claim 9, wherein: the distance between the anode sheet and the cathode sheet is less than or equal to 2.0 mm.

11. The ozone electrolysis structure according to claim 1, wherein: at least one layer of first auxiliary proton exchange membrane is arranged between the anode sheet and the main proton exchange membrane, and the first auxiliary proton exchange membrane is provided with a flow guide hole.

12. The ozone electrolysis structure according to claim 11, wherein: a plurality of shunting holes are formed in the periphery of the flow guide hole on the first auxiliary proton exchange membrane, and are distributed uniformly along the same circumference by taking the center of the flow guide hole as the circle center.

13. The ozone electrolysis structure according to claim 1, wherein: at least one layer of second auxiliary proton exchange membrane is arranged between the cathode sheet and the main proton exchange membrane, and the second auxiliary proton exchange membrane is provided with a flow guide hole.

14. The ozone electrolysis structure according to claim 13, wherein: and a plurality of shunting holes are formed around the diversion hole on the second auxiliary proton exchange membrane, and are uniformly distributed along the same circumference by taking the hole center of the diversion hole as the circle center.

15. The utility model provides an ozone electrolysis chamber, includes the electrolysis chamber body, and the electrolysis chamber body is equipped with water inlet and delivery port, its characterized in that: an ozone electrolysis structure as claimed in any one of claims 1 to 14 is provided in the electrolysis chamber body.

Technical Field

The invention relates to the technical field of ozone electrolysis, and particularly relates to an ozone electrolysis structure and an electrolysis chamber.

Background

Electrolytic cells are commonly used to produce a variety of chemicals, and one of the applications of electrolytic cells is the production of ozone, which is considered an effective disinfectant because it is effective in killing pathogens and bacteria. Meanwhile, the prior art has applied the electrolytic cell to a plurality of fields of generating ozone water, and using the ozone water for medical care disinfection, household sanitation cleaning disinfection, plant and breeding industry disinfection, sewage treatment, and the like.

The basic structure of the existing electrolytic cell for producing ozone or ozone water is that the electrolytic cell consists of an anode and a cathode or consists of an anode, a cathode and a membrane which is clamped in the anode and plays a role of proton exchange, wherein the membrane plays other roles and is not clamped in the electrode. In the latter case, the membranes which function for proton exchange are often single and have the same technical characteristics. The proton exchange efficiency of the proton exchange membrane and the influence of the proton exchange membrane on the running water in the electrolytic chamber can greatly influence the concentration and efficiency of ozone or ozone water prepared in the electrolytic chamber. Obviously, the stronger the proton exchange capacity of the proton exchange membrane, the larger the contact area between the proton exchange membrane and water, the better the water carrying capacity, the lower the indirect energy consumption, and the better the performance of the corresponding electrolysis chamber.

Meanwhile, in the process of preparing ozone or ozone water by electrolyzing water in the electrolytic cell, the distance between the two electrodes and the membrane also determines the speed and efficiency of proton exchange on the proton exchange membrane to a certain extent.

In addition, in the field of ozone production using an electrolytic cell, the problem of scale treatment on the surface of an electrode has become a hot issue of general research in the field. The existing common solution is to open a hole on an electrode which is easy to scale, use pure water as raw water and increase the flow rate of water, thereby promoting the flushing and timely discharging of scale.

Disclosure of Invention

The invention aims to overcome the defects of the prior art, provides an ozone electrolysis structure, solves the technical problems of low ozone preparation efficiency of an electrolytic cell and easy scale deposition on the surface of an electrode, and has the effects of reducing the energy consumption of the electrolytic cell and effectively prolonging the service life.

In order to achieve the purpose, the technical scheme adopted by the invention is as follows:

an ozone electrolysis structure comprises an anode sheet and a cathode sheet which are arranged at intervals, wherein the anode sheet is positioned at a water inlet end, the cathode sheet is positioned at a water outlet end, and a main proton exchange membrane is arranged between the anode sheet and the cathode sheet; the anode sheet is provided with a water inlet, the main proton exchange membrane is provided with a water through hole, and the cathode sheet is provided with a convex structure or a concave structure on the side surface of the water inlet side.

When the ozone electrolysis structure is used, the ozone electrolysis structure is arranged in the electrolysis chamber, when water is electrolyzed, after the water between the anode sheet and the main proton exchange membrane is initially electrolyzed by the anode sheet, one part of the water passes through the water through hole of the main proton exchange membrane to reach the gap between the main proton exchange membrane and the cathode sheet for electrolysis, and the other part of the water passes through the annular gap between the anode sheet and the main proton exchange membrane and then enters the gap between the main proton exchange membrane and the cathode sheet for electrolysis; the water electrolyzed by the cathode plate flows out from the annular gap between the main proton exchange membrane and the cathode plate, and collides with the convex structure or the concave structure to generate water flow vortex in the washing process, and the water flow vortex washes the surface of the cathode plate, so that the scale on the surface of the electrode is easier to wash away, the scale accumulation on the surface of the electrode is avoided, and the service life of the electrode is prolonged; meanwhile, the water inlet holes and the water through holes can enhance the mobility of water flow in the electrolytic chamber, so that the ozone preparation efficiency is improved, and the electrolytic energy consumption is reduced.

In conclusion, when the ozone water preparation device is used for preparing ozone water, scale accumulation on the surface of an electrode can be avoided, the service life of the electrode is prolonged, the ozone preparation efficiency is improved, the electrolysis energy consumption is reduced, and the ozone water preparation device has the advantages of high ozone water concentration, low energy consumption and long service life.

As an improvement of the invention, the side surface of the main proton exchange membrane on the water inlet side is provided with a convex structure or a concave structure.

As an improvement of the present invention, the projection structure includes at least one of a rectangular projection, a circular projection, a trapezoidal projection, an elliptical projection, a triangular projection, an arrow-shaped projection, a star-shaped projection, and an irregularly-shaped projection.

Further, protruding structure is arrow point shape arch, and arrow point shape arch sets up along the radial direction of limbers, and the bellied arrow head of arrow point shape is outwards.

As an improvement of the invention, the number of the convex structures is a plurality, and the convex structures are uniformly distributed along the same circumference by taking the center of the limber hole as the circle center.

As a refinement of the invention, at least one of the anode sheet and the cathode sheet is a diamond sheet.

As a modification of the present invention, the recess structure includes at least one of a rectangular recess, a circular recess, a trapezoidal recess, an oval recess, a triangular recess, an arrow-shaped recess, a star-shaped recess, and an irregularly-shaped recess.

As an improvement of the present invention, the recessed structure is an arrow-shaped recess, and the arrow-shaped recess is arranged along a radial direction of the water passage hole, and an arrow of the arrow-shaped recess faces outward.

As an improvement of the invention, the number of the concave structures is a plurality, and the concave structures are uniformly distributed along the same circumference by taking the center of the water through hole as the center of a circle.

As an improvement of the invention, the ratio of the distance between the anode sheet and the main proton exchange membrane to the distance between the cathode sheet and the main proton exchange membrane is 1: 3.

As an improvement of the invention, the distance between the anode sheet and the cathode sheet is less than or equal to 2.0 mm.

As an improvement of the invention, at least one layer of first auxiliary proton exchange membrane is arranged between the anode sheet and the main proton exchange membrane, and the first auxiliary proton exchange membrane is provided with a diversion hole.

Furthermore, a plurality of shunting holes are formed in the periphery of the flow guide hole on the first auxiliary proton exchange membrane, and the shunting holes are uniformly distributed along the same circumference by taking the center of the flow guide hole as the circle center.

As an improvement of the invention, at least one layer of second auxiliary proton exchange membrane is arranged between the cathode sheet and the main proton exchange membrane, and the second auxiliary proton exchange membrane is provided with a diversion hole.

Furthermore, a plurality of shunting holes are formed in the periphery of the flow guide hole on the second auxiliary proton exchange membrane, and the shunting holes are uniformly distributed along the same circumference by taking the center of the flow guide hole as the circle center.

The invention also provides an ozone electrolysis chamber.

In order to achieve the purpose, the technical scheme adopted by the invention is as follows:

an ozone electrolysis chamber comprises an electrolysis chamber body, wherein the electrolysis chamber body is provided with a water inlet and a water outlet, and an ozone electrolysis structure is arranged in the electrolysis chamber body.

Compared with the prior art, the technical scheme of the invention has the following innovation points and beneficial effects:

when the ozone water preparation device is used for preparing ozone water, scale accumulation on the surface of an electrode can be avoided, the service life of the electrode is prolonged, the ozone preparation efficiency is improved, the electrolysis energy consumption is reduced, and the ozone water preparation device has the advantages of high ozone water concentration, low energy consumption and long service life;

the plurality of proton exchange membranes are connected in series, so that the voltage on the voltage membrane can be reduced, the phenomenon that the membrane is broken, damaged or even scrapped when the working voltage is high is avoided, the service life is indirectly prolonged, and the raised structure or the recessed structure on the proton exchange membranes is beneficial to improving the solubility of ozone gas and effectively improving the concentration of ozone;

through set up protruding structure or sunk structure on the negative pole piece, make the negative pole piece surface unevenness, rivers take place the striking with protruding structure or sunk structure and produce the rivers swirl, and the rivers swirl washes away the negative pole piece surface to wash away electrode surface incrustation scale more easily, and accelerate reaction product exhaust speed.

Drawings

In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the structures shown in the drawings without creative efforts.

FIG. 1 is a schematic structural view of an ozone electrolysis structure of example 1 of the present invention;

FIG. 2 is a schematic structural view of an ozone electrolysis structure of example 2 of the present invention;

description of reference numerals:

10-anode sheet, 11-water inlet hole, 20-cathode sheet, 21-convex structure or concave structure, 30-main proton exchange membrane, 31-convex structure or concave structure, 32-water through hole, 40-first auxiliary proton exchange membrane, 41-flow guide hole, 42-shunt hole, 50-second auxiliary proton exchange membrane, 51-flow guide hole and 52-shunt hole.

The implementation, functional features and advantages of the objects of the present invention will be further explained with reference to the accompanying drawings.

Detailed Description

The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.

It should be noted that, if directional indications (such as up, down, left, right, front, and back … …) are involved in the embodiment of the present invention, the directional indications are only used to explain the relative positional relationship between the components, the movement situation, and the like in a specific posture (as shown in the drawing), and if the specific posture is changed, the directional indications are changed accordingly.

In addition, if there is a description of "first", "second", etc. in an embodiment of the present invention, the description of "first", "second", etc. is for descriptive purposes only and is not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include at least one such feature. In addition, technical solutions between various embodiments may be combined with each other, but must be realized by a person skilled in the art, and when the technical solutions are contradictory or cannot be realized, such a combination should not be considered to exist, and is not within the protection scope of the present invention.

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