Electrolytic sewage treatment device

The electrolytic wastewater treatment device, with its multi-layer overflow structure and staggered electrode plate design, solves the problem of electrode plate clogging and improves treatment efficiency and equipment stability.

CN223576200UActive Publication Date: 2025-11-21YONGXING HUIYOU NEW MATERIAL TECH CO LTD
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Patent Information

Application Number
CN202423151126.7
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-12-19
Publication Date
2025-11-21
Estimated Expiration
2034-12-19

AI Technical Summary

Technical Problem

The existing electrolytic wastewater treatment device has an unreasonable structural design, which makes the electrode plate surface easy to clog, affecting the water flow and reducing the equipment's treatment capacity.

Method used

The design employs a multi-layer overflow structure and staggered positive and negative electrode plates to increase the contact probability between wastewater and the electrode plates, and ensures that impurities are discharged smoothly by reserving sludge discharge channels and pipes.

Benefits of technology

It improved the sewage treatment effect, extended the equipment maintenance time, and increased the treatment capacity per unit time.

✦ Generated by Eureka AI based on patent content.

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    Figure CN223576200U_ABST
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Abstract

The utility model discloses an electrolytic sewage treatment device, which comprises a support frame, a reaction tank, a water tank and a water tank, the gas collecting hood is arranged above the reaction tank, and an exhaust pipe is arranged at the top of the gas collecting hood; the copper bar is arranged on the side wall of the reaction tank; the electrode group is inserted and mounted in the reaction tank and is connected with the copper bar through a bolt; the direct-current power supply is arranged on one side of the supporting frame and used for supplying power to the copper bar; the water inlet pipe is arranged at the bottom of the reaction tank and communicated with one end of the reaction tank; the water outlet pipe is arranged at the bottom of the reaction tank and communicated with the other end of the reaction tank. The sewage treatment device has the beneficial effects that the multilayer overflow structure is matched with the electrode group to treat sewage, the contact probability between the sewage and the polar plate can be increased, so that the sewage treatment effect is improved, meanwhile, by reserving the deslagging channel and the deslagging pipe, impurities filtered out from the sewage can be smoothly discharged, the maintenance time of the device is prolonged, and the service life of the device is prolonged. The sewage treatment capacity of the equipment is improved.
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Description

TECHNICAL FIELD

[0001] The utility model relates to sewage treatment technical field, concretely relates to a kind of electrolytic sewage treatment device. BACKGROUND

[0002] Electrolytic sewage treatment technology is a method for removing pollutants in water using electrolysis principle. It promotes the oxidation of pollutants at the anode or the reduction reaction at the cathode by applying current to the electrode, and converts it into harmless substances. This technology is valued for its high efficiency, environmental protection and recyclable useful substances. With the continuous optimization of electrode materials and reactor design, the treatment efficiency of electrolysis method is improved, and the cost is reduced, becoming one of the important technologies in the field of sewage treatment.

[0003] Research has found that the current electrolytic sewage treatment device has defects, mainly due to unreasonable structure design, the existing electrolytic positive and negative electrode plates and electrolytic cell are not targeted for sewage treatment, which often causes the electrolytic sewage to be blocked in the conveying process. The surface of the electrode plate affects the water flow through effect, reduces the processing capacity of the equipment per unit time, and cannot meet the current production demand. UTILITY MODEL CONTENT

[0004] The utility model discloses a kind of electrolytic sewage treatment devices to solve the above problems, to solve the technical problem that the structure design is not reasonable in prior art, the existing electrolytic positive and negative electrode plates and electrolytic cell are not targeted for sewage treatment, which often causes the electrolytic sewage to be blocked in the conveying process. The surface of the electrode plate affects the water flow through effect, reduces the processing capacity of the equipment per unit time, and cannot meet the current production demand. In the preferred technical solution of the many technical solutions provided by the utility model, the sewage is treated by the multi-layer overflow structure and the electrode group, which can increase the contact probability between the sewage and the electrode plate, thereby improving the effect of sewage treatment. At the same time, by reserving the deslag discharge channel and the deslag pipe, the impurities filtered out of the sewage can be smoothly discharged, the maintenance time of the equipment is prolonged, and the sewage treatment capacity of the equipment is improved. The technical effects are described in detail below.

[0005] To achieve the above object, the utility model provides the following technical scheme:

[0006] The utility model provides an electrolytic sewage treatment device, which comprises:

[0007] Support frame, the upper portion of the support frame is provided with a reaction tank;

[0008] Gas collecting hood, arranged above the reaction tank, the top of the gas collecting hood is provided with an exhaust pipe;

[0009] Copper bar, arranged on the side wall of the reaction tank;

[0010] The electrode group is inserted into the reaction tank and connected with the copper bar through bolts;

[0011] The direct current power supply is arranged on one side of the support frame and used for supplying power to the copper bar;

[0012] The water inlet pipe is arranged at the bottom of the reaction tank and communicated with one end of the reaction tank.

[0013] The water outlet pipe is arranged at the bottom of the reaction tank and communicated with the other end of the reaction tank.

[0014] Preferably, the inner bottom surface of the reaction tank is provided with a slag discharge channel, and the inner bottom surface of the reaction tank is provided with a slag discharge pipe connected with the slag discharge channel.

[0015] Preferably, the electrode group comprises positive electrode plates and negative electrode plates, and the positive electrode plates and the negative electrode plates are arranged alternately and inserted into the reaction tank.

[0016] Preferably, the inner wall of the reaction tank is provided with a groove for inserting the electrode group.

[0017] Preferably, the reaction tank is internally provided with a vertically arranged water level control plate, and the reaction tank is internally provided with uniformly distributed water blocking plates.

[0018] Preferably, the lower part of the reaction tank is provided with a cooling water pipe for cooling the direct current power supply.

[0019] The beneficial effects are that:

[0020] The sewage is treated by the multi-layer overflow structure and the electrode group, so that the contact probability between the sewage and the electrode plates is increased, the sewage treatment effect is improved, the impurities filtered out from the sewage can be smoothly discharged through the reserved slag discharge channel and the slag discharge pipe, the maintenance time of the equipment is prolonged, and the sewage treatment capacity of the equipment is improved. BRIEF DESCRIPTION OF DRAWINGS

[0021] In order to more clearly illustrate the technical scheme in the embodiments of the present application or the prior art, the drawings needed to be used in the following embodiment or prior art description will be briefly introduced. Obviously, the drawings in the following description are only some embodiments of the present application, and those skilled in the art can also obtain other drawings according to these drawings without creative labor.

[0022] Figure 1 is a perspective view of the utility model Figure One ;

[0023] Figure 2 is a perspective view of the utility model Figure Two ;

[0024] Figure 3It is the perspective view of the three-dimensional structure of the utility model Figure Three ;

[0025] Figure 4 It is the front view of the utility model;

[0026] Figure 5 It is the internal section view of the reaction tank of the utility model;

[0027] Figure 6 It is the top view of the reaction tank of the utility model;

[0028] Figure 7 It is the structure view of the positive plate of the utility model;

[0029] Figure 8 It is the structure view of the negative plate of the utility model.

[0030] The sign of the drawing is explained as follows:

[0031] 1, water outlet pipe; 2, reaction tank; 3, copper bar; 4, exhaust pipe; 5, gas collecting cover; 6, direct current power supply; 7, support frame; 8, cold clean water pipe; 9, water inlet pipe; 10, slag discharge pipe; 11, slag discharge channel; 12, electrode group; 1201, positive plate; 1202, negative plate; 13, water level control plate; 14, water blocking plate. Specific implementation

[0032] In order to make the purpose, technical scheme and advantage of the utility model more clear, the technical scheme of the utility model will be described in detail below. Obviously, the described embodiment is only a part of the embodiment of the utility model, not all the embodiment. Based on the embodiment in the utility model, all other embodiments obtained by the ordinary skill in the art without making creative labor belong to the scope of the utility model.

[0033] Referring to Figures 1-8 The utility model provides electrolytic sewage treatment device, including:

[0034] Support frame 7, the upper portion of support frame 7 is provided with reaction tank 2, and reaction tank 2 top is opened, which is convenient for subsequent cleaning;

[0035] Gas collecting cover 5 is arranged above reaction tank 2, and the top of gas collecting cover 5 is provided with exhaust pipe 4; during sewage treatment, the gas generated by reaction is collected through gas collecting cover 5 and is led out to external gas treatment equipment through exhaust pipe 4 for treatment;

[0036] Copper bar 3 is arranged on the side wall of reaction tank 2, and current is dispersed to each electrode group 12 through copper bar 3 for power supply, so as to cooperate with chemical reaction;

[0037] The electrode group 12 is plug-in mounted in the reaction tank 2 and connected with the copper bar 3 through bolts. The electrode group 12 is divided into positive electrode plates 1201 and negative electrode plates 1202, which are arranged alternately in the reaction tank 2. The surface of the electrode plates in the electrode group 12 is provided with through holes for water flow, which can not only play a filtering role, but also increase the probability of contact between the electrode plates and sewage, thereby improving the sewage treatment effect. The positive electrode plates 1201 adopt a tensile net structure, and the negative electrode plates 1202 adopt a punched plate structure. Such a structure design can guide the water flow to pass through the net holes in an orderly manner, thereby improving the reaction efficiency.

[0038] The direct current power supply 6 is arranged on one side of the support frame 7 and used for supplying power to the copper bar 3. The direct current power supply 6 is connected with the mains and introduced into the copper bar 3 after voltage transformation.

[0039] The water inlet pipe 9 is arranged at the bottom of the reaction tank 2 and connected with one end of the reaction tank 2. The sewage is introduced into the water inlet pipe 9 through the water pump and finally flows into the reaction tank 2 for purification treatment.

[0040] The water outlet pipe 1 is arranged at the bottom of the reaction tank 2 and connected with the other end of the reaction tank 2. The purified sewage passes through the reaction tank 2 and finally leaves the reaction tank 2 to realize batch treatment of the sewage.

[0041] In use, the sewage is introduced into the reaction tank 2 from the water inlet pipe 9 and contacts the electrode group 12 when passing through the reaction tank 2. At the same time, the direct current power supply 6 supplies power to the electrode group 12 through the copper bar 3 to facilitate chemical reaction, thereby reducing the heavy metal ions in the sewage. The through holes on the surface of the electrode group 12 screen the recesses, thereby filtering out the waste residues. Finally, the treated sewage is introduced into the water outlet pipe 1 to realize complete treatment of the sewage.

[0042] In another embodiment, the inner bottom surface of the reaction tank 2 is provided with a residue discharge channel 11, and the inner bottom surface of the reaction tank 2 is provided with a residue discharge pipe 10 connected with the residue discharge channel 11. Since the sewage is in constant contact with the electrode group 12 during the treatment process, the sewage is often screened out by the through holes on the surface of the electrode group 12 and gradually falls to the bottom of the reaction tank 2 under the action of gravity. In order to facilitate the filtered waste residues to be quickly discharged out of the reaction tank 2, the bottom edge of the electrode group 12 is still away from the bottom of the reaction tank 2 after being installed in the reaction tank 2, i.e. the residue discharge channel 11. The waste residues after reaction are introduced into the residue discharge pipe 10 through the residue discharge channel 11 and finally discharged out of the equipment. Through the design of the residue discharge structure, the efficiency of residue discharge during the sewage treatment process can be significantly improved, thereby ensuring the treatment capacity.

[0043] In another embodiment, the inner wall of the reaction tank 2 is provided with a groove for inserting the electrode group 12. The groove can cooperate with the electrode plate in the electrode group 12 to position the electrode group 12. This design can reduce the installation difficulty during insertion and improve the stability of the electrode group 12, so that the electrode group 12 can always be inside the groove during the subsequent sewage treatment process to maximize the contact area with the sewage.

[0044] In another embodiment, the reaction tank 2 is internally provided with a vertically installed water level control plate 13, and the reaction tank 2 is provided with evenly distributed water blocking plates 14. The number of water blocking plates 14 is three, and the electrode group 12 is internally installed. The height of the water level control plate 13 is higher than the height of the water blocking plate 14. After the sewage to be treated is introduced into the reaction tank 2 through the water inlet pipe 9, it will first accumulate in the gap between the reaction tank 2 and the water level control plate 13. When the amount of sewage is large enough, it will overflow from the top of the water level control plate 13 into the gap between the water blocking plate 14 and the water level control plate 13, and then contact the electrode plate group. During the contact process, the water flow flows through the mesh and perforations of the positive and negative electrode plates to realize the chemical reaction of sewage treatment. Finally, after moving through multiple water blocking plates 14, the sewage is discharged from the water outlet pipe 1 to realize the whole sewage flow process.

[0045] In another embodiment, the lower part of the reaction tank 2 is provided with a cooling water pipe for cooling the direct current power supply 6. The cooling water pipe is used to continuously cool the direct current power supply 6 to improve the stability of the equipment.

[0046] The above is only a specific embodiment of the present application, but the protection scope of the present application is not limited thereto. Any skilled person in the art can easily think of changes or replacements within the technical range disclosed by the present application, which should be covered by the protection scope of the present application. Therefore, the protection scope of the present application should be subject to the protection scope of the claims.

Claims

1. An electrolytic sewage treatment device, characterized by: The utility model relates to a direct current electrolysis device for producing hydrogen peroxide, which comprises: a support frame (7) provided with a reaction tank (2) on top; a gas collecting hood (5) provided above the reaction tank (2), the top of which is provided with an exhaust pipe (4); a copper bar (3) provided on the side wall of the reaction tank (2); an electrode group (12) inserted and installed in the reaction tank (2) and connected with the copper bar (3) through bolts; a direct current power supply (6) provided on one side of the support frame (7) for supplying power to the copper bar (3); a water inlet pipe (9) provided at the bottom of the reaction tank and connected at one end of the reaction tank (2); a water outlet pipe (1) provided at the bottom of the reaction tank and connected at the other end of the reaction tank (2).

2. The electrolytic sewage treatment device according to claim 1, characterized by: The inner bottom surface of the reaction tank (2) is provided with a slag discharge channel (11), and the inner bottom surface of the reaction tank (2) is provided with a slag discharge pipe (10) connected with the slag discharge channel (11).

3. The electrolytic sewage treatment device according to claim 1, characterized by: The electrode group (12) is divided into positive electrode plates (1201) and negative electrode plates (1202), which are installed in the reaction tank (2) in an interleaved manner.

4. The electrolytic waste water treatment device according to claim 1, characterized by: The inner wall of the reaction tank (2) is provided with a groove for inserting the electrode group (12).

5. The electrolytic waste water treatment device according to claim 1, characterized by: The reaction tank (2) is provided with a vertically installed water level control plate (13) inside, and the reaction tank (2) is provided with evenly distributed water blocking plates (14).

6. The electrolytic waste water treatment device according to claim 1, characterized by: The lower part of the reaction tank (2) is provided with a cooling water pipe (8) for cooling the direct current power supply (6).